Text

Golder Associates Inc. - Thermal Discharge Study (Bound)
	ML100830443
Person / Time
Site:	Saint Lucie
Issue date:	01/21/2010
From:	; Golder Associates
To:	; Florida Power & Light Co, Office of Nuclear Reactor Regulation
References
	EPP 3.2.4, L-2010-059 093-87687
	Download: ML100830443 (106)
	v • d • e

7 THERMAL DISCHARGE STUDY In Support of NPDES Modification Request Florida Power & Light St. Lucie Plant NPDES Permit No. FL0002208 Submitted To:

Submitted By:

Florida Power & Light Company 700 Universe Boulevard Juno Beach, FL 33408 Golder Associates Inc.

6026 NW 1st Place Gainesville, FL 32607 USA Distribution:

January 21, 2010 093-87687 e'G

' Associates

January 2010 093-87687 Table of Contents 1.0 IN T R O D U C T IO N...............................................................................................................................

1 2.0 MODELING METHODS.............

2 3.0 MODEL RESULTS 3

3.1 T e m p e ra tu re...................................................................................................................................

3 3.2 T im e /T e m p e ra tu re.........................................................................................................................

4 3.3 D isso lve d O x yg e n.........................................................................................................................

4 3.4 T herm al Plum e V ertical Profile.................................................................................................

4 4.0 HISTO RICA L BENTHIC STUDIES..............................................................................................

5 5.0 SUM M ARY AND CO NC LUSIO NS..............................................................................................

8 6.0 R E F E R E N C E S..................................................................................................................................

9 List of Tables Table 1 Comparison of Thermal Plume for the Y-Nozzle Diffuser Table 2 Y-Nozzle Volume Enclosed vs. Temperature - Cubic Feet Table 3 Multiport Volume Enclosed vs. Temperature - Cubic Feet Table 4 Combined Volume Enclosed vs. Temperature - Cubic Feet List of Figures Figure 1 Probability That Intake Temperature Will be Equaled or Exceeded Figure 2 Y-Nozzle Enclosed Volumes vs. Water Temperatures Figure 3 Multiport Enclosed Volumes vs. Water Temperatures Figure 4 Enclosed Volume vs. Water Temperature - FPL St. Lucie Plant Figure 5 Increase in Enclosed Volumes Due to Proposed Increase in Maximum Discharge Temperature Figure 6 Areal Extent of Thermal Plumes Figure 7 Time/Temperature Relationship Figure 8 Thermal Plume Vertical Profile (96°F isotherm) for Multiport Diffuser Figure 9 Thermal Plume Vertical Profile (96°F isotherm) for Y-Nozzle Diffuser List of Appendices Appendix A Calculation 16 Appendix B Calculation 18 report-ps,-li 5.docx A soldates

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093-87687

1.0 INTRODUCTION

Florida Power & Light Company (FPL) plans to submit a request to modify the National Pollutant Discharge Elimination System (NPDES) permit for the St. Lucie Nuclear Power Plant (St. Lucie Plant);

specifically to increase the maximum heated water temperature at the point of discharge for Outfall D-001 from 113 degrees Fahrenheit (OF) to 115°F.

This modification may be necessary as the result of an intake water temperature analysis performed, which indicates that the upper 1-percent intake water temperature is estimated to be 86.3°F (Figure 1). Assuming a full load temperature rise of the uprated St. Lucie Plant facility of 28.6°F, an intake temperature of 86.30F results in a discharge temperature of 114.9°F. Rounding up for conservatism and ease of computation, Golder Associates Inc. (Golder) has modeled the thermal plume assuming a discharge temperature of 11 50F.

The potential biological impact of the thermal discharge increase from 113 0F to 115 0F was evaluated using historical studies in the vicinity of the St. Lucie Plant discharge.

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093-87687 2.0 MODELING METHODS This report includes model calculations that were conducted to estimate higher thermal discharge temperatures and associated thermal plume results. This thermal modeling assessment was conducted to analyze both the existing thermal discharge plumes and the expected thermal discharge plumes that would result from the increased discharge temperature of 115'F. The model used was MULDIF, which is the Envirosphere version of the near-field Koh and Fan model.

Appendix 10.6 of the St. Lucie Plant Uprate Site Certification Application (SCA) includes a listing of the program and previous calculations, as well as a discussion of the historical verification of the model. The calculations presented in this report are the additional model runs conducted for this evaluation, and they were:

N Calculation 16-MULDIF Run - Y-nozzle with 115 0F Discharge Temperature (Appendix A)

II Calculation 18 - Isotherm Sizes and Plume Delineation (Appendix B)

The Koh and Fan near-field model is a submerged jet model consisting of a set of seven simultaneous differential equations.

They include equations of conservation of mass, horizontal momentum flux, vertical momentum flux, density deficiency flux, thermal energy flux, and two equations of horizontal and vertical distance. The solution of these equations provides jet width, dilution, temperature, density, jet trajectory, and temperature rise as a function of position.

Golder

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093-87687 3.0 MODEL RESULTS 3.1 Temperature The model results, based on Calculation 16, indicate that the thermal plume does not change in size when measured by temperature rise above ambient. The increase in discharge water temperature is caused by a corresponding increase in ambient water temperature. The model results show that the change in water density of the discharge is of the same magnitude as the change in water density of the ambient water. The buoyant force involved is measured by the densimetric Froude Number Fd, defined as:

1/2 Fd = Uo / (((Pambient -- Pdischarge) / Pambient) x g x D)

, where:

U0

= jet discharge velocity Pambient

= density of ambient water Pdischarge

= density of discharge water g

= gravitational constant D

= nozzle diameter Only the ambient and discharge densities are changing, and the changes in those parameters resulting from the increase of 2°F are so small that the predicted thermal plume characteristics are almost unchanged from what was presented in the most recent minor permit revision application. Therefore, it was assumed that the thermal plume resulting from the 11 5°F discharge water is the same as that from the 113 0F water except that the water temperature is 20F higher at any given location. Table 1 shows the results for the Y-nozzle upon which this conclusion was made.

However, biological systems respond to absolute temperature as well as to temperature rise.

The thermal plume from the 115 0F discharge is slightly larger than that for 113 0 F with respect to absolute temperature. The relative volumes of each isotherm after the first step for the Y-nozzle diffuser down to 96 0F are tabulated in Table 2 and plotted in Figure 2. Similarly, the relative volumes of each isotherm after the first step for the multiport diffuser are tabulated in Table 3 and plotted in Figure 3.

Table 4 tabulates the combined volumes for both diffusers and Figure 4 shows the same information graphically. Figure 5 illustrates the increased water volumes due to the proposed increased discharge temperature relative to the water volumes due to the existing permitted maximum discharge temperature.

The maximum areal extent of the 96 0F isotherm, projected to the water. surface, is depicted in Figure 6 for both diffusers. As shown in Figure 6, the additional ambient water affected by the increased absolute temperature is minimal as well; less than 25 feet in any direction for the Y-nozzle diffuser and less than 6 feet in any direction for the multiport diffuser.

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093-87687 3.2 Time/Temperature Because the time/temperature relationship is similar for both diffusers, only the Y-nozle diffuser has been analyzed.

The time/temperature relationship is shown in Figure 7.

If a particle of water were entrained into the center of the plume at the hottest temperature of 115 0F, it would be cooled down to 960F within about 12.5 seconds. The relationship for the Y-nozzle would be of the same magnitude, i.e.,

measured in seconds.

3.3 Dissolved Oxygen During the most recent minor permit revision application process for the St. Lucie Uprate Project, a relationship was developed between water temperature and water saturated dissolved oxygen.

The estimated values of saturated dissolved oxygen at the two discharge temperatures evaluated were:

The difference in saturated dissolved oxygen level between these two temperatures is not measurable.

3.4 Thermal Plume Vertical Profile Figure 8 illustrates the vertical profile of the thermal plume for the multiport diffuser. As shown, the multiport diffuser is located about 8 feet above sea bottom. The thermal discharge dissipates in the water column and does not come in contact with benthic organisms in the sea bottom. Figure 9 illustrates the thermal plume vertical profile for the Y-nozzle diffuser. This diffuser discharges in an area where the sea bottom was excavated to about 6 feet below sea bottom. As shown in Figure 9, the model predicts that the 96°F isotherm will not come in contact with the sea bottom.

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093-87687 4.0 HISTORICAL BENTHIC STUDIES Benthic macro-invertebrate communities are composed of animals that live on or in the sea floor. They are an important link in marine food webs as they feed on detritus, organic matter, and other invertebrates in the sediments and are preyed upon by larger macro-invertebrates and fish species that forage in the benthic environment. Furthermore, this faunal group can be an important indicator of water quality and environmental conditions.

Shifts in the physical environment alter the competitive advantage among macro-invertebrates and can result in alterations to the community composition reflected in the diversity and abundance of component species.

Benthic studies were initially conducted in the vicinity of the St. Lucie Plant in 1969 and 1970. These studies were focused on identifying economic resources that could potentially be impacted by Plant construction and operation.

The initial field effort in February 1969 included diver observations at 35 stations located up to 6 miles from the St. Lucie Plant. The second field effort (June 1969) included only 11 sites, nine of which were within approximately 2 miles of the Plant and two of which were just over 6 miles away. This sampling effort included diver observations as well as benthic dredges and collection of sediment samples for the identification of macro-invertebrates.' The final sampling event included diver observations at 16 stations that were located generally within I mile of the St. Lucie Plant (Ebasco, 1970).

Conditions at all stations were conducive to diver observations with generally good water clarity. The only commercially important species observed were Calico scallops (Argopecten gibbus); however, these were observed in relatively low densities and quite distant from established scallop beds. The benthic habitat at all stations was composed of sand or sand and shell. No grass or macro-algae, and no rock formations or coral reefs were identified. Data from the benthic grabs showed a typical array of sub-littoral species.

The predominant macro-invertebrates were polychaete worms, barnacles, amphipods, bryozoans, echinoderms, chitons, and slipper shells. The benthic sampling component of this study noted a higher diversity and abundance of macro-invertebrates at four stations that had higher concentrations of shells and shell hash in the sediments. This relationship is further confirmed in later-studies focused primarily on ecological rather than economic impacts. The report concluded that the discharge of heated effluent was unlikely to impact commercial or sport fishery operations in the area studied (Ebasco, 1970).

Pre-operational baseline studies of the benthos were conducted from 1971 to 1973.

Sampling was conducted in three offshore environments: the beach terrace (approximately 8 meters deep), offshore trough (approximately 11 meters deep), and an offshore shoal (Pierce Shoal, approximately 7 meters deep) (Florida Marine Research, 1977).

Each habitat type was characterized by unique physical characteristics. The beach terrace experiences high wave energy and had "fine to very fine, moderately well sorted, gray terrigenous sand, often well compacted." One station was located on the beach terrace.

The trough zone is offshore of the beach terrace and slightly deeper. It therefore receives less wave rp Golder report-psi-115.dor~x

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January 2010 6

093-87687 energy and has more poorly sorted sediments. Sediments were composed of "very coarse, poorly sorted sand containing very little mud, and with numerous large shell fragments." Three sampling stations were located in the trough zone.

The final benthic sampling station was located on Pierce Shoal, approximately 2 miles offshore. Sediments were "medium grained, moderately well sorted calcareous sand."

Each of the three habitats was found to have a unique species assemblage as determined by their physical habitat characteristics. The beach terrace station was described as having a depauperate group of transient species; the trough zone as a rich but fluctuating assemblage having few dominant species; and the shoal as a less rich but fairly permanent and characteristic fauna. Dominant arthropods on the shoal included haustoriid and phoxocephalid amphipods, which are taxa characteristic of harsh, shifting sand habitats. Overall the area was characterized as having low diversity and low density and being of a transient nature.

Much of this was attributed to the study area's location along the transitional zone between temperate, tropical, and sub-tropical climates with influences from various currents, including water masses from the Indian River Lagoon via the St. Lucie inlet located south of the St. Lucie Plant (Florida Marine Research, 1977).

Benthic monitoring was again conducted when Unit 1 became operational in 1976 to determine if there were impacts from the discharge of heated water of the Y-nozzle diffuser.

Sampling stations were consistent with those monitored during pre-operational studies with the addition of a second beach terrace site south of the St. Lucie Plant and in a location outside the area of influence of the Plant's discharge.

This monitoring was conducted quarterly through 1982.

In general, the trough stations exhibited the highest diversity and abundance of benthic macro-invertebrates (Applied Biology, 1983) and the taxa at these stations were correlated with temperature (Applied Biology, 1981). The taxa observed at both the shoal and beach terrace stations were not correlated with temperature and were more likely controlled by other physical factors such as substrate type, currents, and disturbance by wave action (Applied Biology, 1981). Across all stations, density and diversity tended to be the highest during the summer and lowest during the spring (Applied Biology, 1983).

Though there were intra-and inter-annual variations in the biological communities monitored, there were no significant differences from the pre-operational baseline that could be attributed to the St. Lucie Plant operations.

Significant dissimilarity was detected among stations in 1981; however, it seemed to be consistent with shifts in dominant taxa due to natural variation and patchy larval settlement within the benthic community rather than a Plant effect (Applied Biology, 1981). No shifts in dominant taxa were observed that were associated with Plant operation.

Sampling was expanded in 1982 when the US Environmental Protection Agency (EPA) assumed jurisdiction over the biological monitoring program. The sampling plan was revised to investigate potential report-psi-115.docx C

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093-87687 new impacts with the addition of Unit 2 and the discharge of heated water from the newly-installed multiport diffuser.

Quarterly monitoring was conducted at seven stations: four stations from the 1976-1982 studies were retained and three additional stations in closer proximity to the discharge pipes were added (Applied Biology, 1983).

The result is a more fine scale gradient of decreasing thermal effects than was sampled from 1976 to 1982. Sampling at these locations was conducted quarterly from May 1982 to mid-1984.

Similar to the studies from 1976-1982, two unique community assemblages were identified in the beach terrace and offshore trough zones.

The communities present in the trough, sand, and shell habitat exhibited more stability over the course of the study. Macro-invertebrate assemblages on the beach terrace exhibited more variability; however, variations in density and abundance were not correlated with the water quality properties influenced by the discharge of cooling water from the St. Lucie Plant (temperature, dissolved oxygen, or turbidity) [Ecological Associates, Inc. (EAI), 2001].

Stations adjacent to the multiport diffuser (both up-and down-current from the prevailing plume direction) that were in the offshore trough did show a slow decline in the diversity and abundance of macro-invertebrates. This corresponded to occasional increases in fine-grained particles in the area of the discharge. These accumulations were temporary in nature and readily dispersed by currents and wave action.

It has been hypothesized (EAI, 2001) that there is a connection between benthic communities and sediment stability.

Turbulence and scouring, suspension, and settling of sediments associated with the discharge structures may prevent the establishment of stable benthic communities in the immediate vicinity of the discharge pipes. Figure 6 shows the historical locations of benthic sampling stations.

The discharge of heated water from the operation of Units 1 and 2 of the St. Lucie Plant has demonstrated only minimal impacts to the benthic environment, both in scope and severity. The thermal modeling conducted as part of this study indicates that there will be no measurable change in thermal exposure of benthic organisms in the vicinity of the discharges, because the plume is buoyant and is expected to float away from the sediments as it mixes (see Figures 8 and 9).

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093-87687 5.0

SUMMARY

AND CONCLUSIONS The difference in the extent of the thermal plume attributable to the increase in discharge temperature from 113 0F to 115 0F is relatively small.

For the Y-nozzle diffuser, the increase ranges from about 2,000 cubic feet at the highest temperature (111°F) to about 1,000 cubic feet at the lowest temperature (96°F). For the multiport diffuser, the range is on the order of 50 cubic feet at 111 OF to 350 cubic feet at 960F.

The heated water exiting the diffusers at 115'F would be cooled down to 96 0F within about 12.5 seconds. The potential decrease in dissolved oxygen concentration due to the increase in discharge temperature is on the order of about 0.01 milligram per liter.

The proposed change in the thermal discharge will increase the temperature of a small volume of the Atlantic Ocean water column in the near vicinity of the St. Lucie Plant discharge. The proposed thermal discharge is expected to quickly mix with the Ocean waters and is expected to interact with the bottom sediments in a similar manner as the currently permitted discharge; the heated water will float as it mixes.

Fish and other motile marine organisms are able to avoid heated discharges by swimming away from their source. Fish have also been observed to be attracted to heated discharges without measurable harm.

Benthic organism communities are sedentary and cannot avoid the changes in water temperature. Based on the thermal modeling conducted, no measurable change in thermal exposure is anticipated for benthic organisms because the plume is buoyant and the model predicts that it will float away from the sediments as it mixes. The multiport discharges are located from 7 to 9 feet above sea bottom, allowing the water to rise as it mixes with minimal interaction with benthic organisms. The Y-nozzle discharges are at the sea bottom, but rise while mixing with ambient water within the area of the sea bottom that was excavated for the Y-nozzle diffuser installation.

Golder concludes that the potential biological impacts of the proposed discharge temperature change are minimal and not measurable.

GOLDER ASSOCIATES INC.

Harold A. Frediani, Jr., PE # 36394 Isabel C. Johnson, MS Senior Engineer Associate and Senior Consultant HF/tz Golder report-ps,-l 5docx Associates

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093-87687

6.0 REFERENCES

Applied Biology Inc. 1980. FPL St. Lucie Plant Annual Non-Radiological Monitoring Report 1980 Volume 2.

Applied Biology.Inc.

1981.

FPL St. Lucie Plant Annual Non-Radiological Monitoring Report 1981 Appendix. Applied Biology Inc.

Applied Biology Inc.

1983.

FPL St. Lucie Plant Annual Non-Radiological Environmental Monitoring Report 1983.

Ebasco Services Inc.; Lackey JR. 1970. FPL Hutchinson Island Plant Environmental Report - Appendix 3 Hutchinson Island Ecologic Surveys; Appendix 4 Ecological Literature Review.

Ecological Associates, Inc. 2001. Survey of Aquatic Environments Potentially Affected by the Operation of the St. Lucie Power Plant Hutchinson Island, Florida.

Florida Marine Research; Camp, Whiting, and Martin.

1977. Nearshore Marine Ecology at Hutchinson Island, Florida: 1971-1974. Florida Marine Research Publications, number 25.

- Associates report-psi-1 5.docx

TABLES

January 2010 093-87687 TABLE 1 COMPARISON OF THERMAL PLUME FOR THE Y-NOZZLE DIFFUSER Y-Nozzle Thermal Plume with 115°F Discharqe x

T y

T Jet]

_ Width T

46.8400 0.0002 15.1577 24.6679 76.6963 1.6482.

28.9435 12.8708 91.4529 4.0785 35.6492 10.3756 105.9208 7.8602 42.0821 8.6769 119.9264 13.0983 48.1264 7.4391 133.2993 19.7884 53.7111 6.4915 145.9083 27.8275 58.8339 5.7387 Y-Nozzle Thermal Plume with 113 0F Discharge 1

1 Jet Width AT 46.8400 0.0002 15.1577 24.1504 76.7013 1.5821 28.9508 12.6013 91.4735 3.9175 35.6741 10.1593 105.9779 7.5586 42.1426 8.4975 120.0498 12.6169 48.2433 7.2875 133.5237 19.1019 53.9003 6.3617 146.2664 26.9274 59.1015 5.6267 Table 1.docx

January 2010 093-87687 TABLE 2 Y-NOZZLE VOLUME ENCLOSED VS.

TEMPERATURE - CUBIC FEET Temperature Proposed Existing Volume Allowed (OF)

(115'F discharge)

(113'F discharge) by Permit*

111 2,072.09 110 2,116.10 109 2,167.37 2,072.09 108 2,227.35 2,116.10 107 2,297.77 2,167.37 106 2,380.63 2,227.35 105 2,478.32 2,297.77 104 2,593.64 2,380.63 103 2,729.94 2,478.32 12,367,168 102 2,891.21 2,593.64 101 3,082.26 2,729.94 100 3,308.90 2,891.21 99 3,583.19 3,082.26 98 3,938.02 3,308.90 97 4,419.08 3,583.19 96 5,088.63 3,938.02

Volume is for the 170F isotherm above ambient: 101.4 0F for Existing and 103.4°F for Proposed.

Tables-Figures.xlsx

. January 2010 093-87687 TABLE 3 MULTIPORT VOLUME ENCLOSED VS TEMPERATURE - CUBIC FEET Proposed Existing Temperature (115°F (113°F Volume Allowed (OF) discharge) discharge) by Permit*

110 473.88 109 486.45 108 501.25 473.88 107 518.75 486.45 106 539.48 501.25 105 564.12 518.75 104 593.46 539.48 103 628.46 564.12 102 670.27 593.46 101 720.34 628.46 100 780.43 670.27 99 855.12 720.34 98 957.13 780.43 97 1,098.45 855.12 96 1,304.36 957.13 95 1098.451 94 1304.361

Volume is for the 170F isotherm above for Existing and 103.4°F for Proposed.

ambient: 101.4 0F Tables-Figures.xlsx

January 2010 093-87687 TABLE 4 COMBINED VOLUME ENCLOSED VS TEMPERATURE - CUBIC FEET Temperature Proposed Existing Proposed Existing Temperature Existing Proposed Increase OF Y-Nozzle Y-Nozzle Multiport Multiport

,°FExisting PosdIra 111 2,072 111 0

2,072 2,072 110 2,116 474 110 0

2,590 2,590 109 2,167 2,072 486 109 2,072 2,654 582 108 2,227 2,116 501 474 108 2,590 2,729 139 107 2,298 2,167 519 486 107 2,654 2,817 163 106 2,381 2,227 539 501 106 2,729 2,920 192 105 2,478 2,298 564 519 105 2,817 3,042 226 104 2,594 2,381 593 539 104 2,920 3,187 267 103 2,730 2,478 628 564 103 3,042 3,358 316 102 2,891 2,594 670 593 102 3,187 3,561 374 101 3,082 2,730 720 628 101 3,358 3,803 444 100 3,309 2,891 780 670 100 3,561 4,089 528 99 3,583 3,082 855 720 99 3,803 4,438 636 98 3,938 3,309 957 780 98 4,089 4,895 806 97 4,419 3,583 1,098 855 97 4,438 5,518 1,079 96 5,089 3,938 1,304 957 96 4,895 6,393 1,498 Tables-Figures.xlsx

FIGURES

m-n

-m m-m-m

-m

-m-m-m

-m-Figure 1. Probability That Intake Temperature will be Equalled or Exceeded St. Lucie Nuclear - POR 8105 through 9/07 100%

95%

90%

85%

80%

75%/o 70% -

65%

60%--

55%

A l

50%

45%

40%

35%

30%

25%--

20%----

15%

5%

0%

55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 Intake Temperature - Degrees F.

8(

1/6/2010 2:56 PM Figure-1.xlsx Figure 1

mm mmm m- -

n m

Figure 2. Y-Nozzle Enclosed Volumes vs. Water Temperatures

--*.-Proposed...

,,,1--Existing...

6,000 5,000 4,000 u.

S U.

.0 43 3,000 2,000 1,000 0

94 96 98 100 102 104 106 108 110 112 Degrees F Tables-Figures.xtsx

Figure 3. Multiport Enclosed Volumes vs. Water Temperature Proposed...

,-I-Existing...

1,400 1,200 1,000 0

SL

'a JU I-'

800 600 400 200 0

92 94 96 98 100 102 104 106 108 110 Degrees F 112 Tables-Figures.xlsx

m m

m n

-m m

m n-m m

Figure 4. Enclosed Volume vs. Water Temperature FPL St. Lucie Plant Existing

-,m-Proposed 7,000 6,000 5,000 U

C-a.

E 4,000 0

3,000

.0

.a 3,000 1,00 94 96 98 100 102 104 106 108 110 112 Degrees F.

Tables-Figures.xlsx

Figure 5. Increase in Enclosed Volumes Due to Proposed Increase in Maximum Discharge Temperature 3,000 2,750 2,500 2,250 2,000 1,750 u_

S1,500 U

1,250 1,000 750 500 250 0

96 97 98 99 100 101 102 103 104 105 106 107 108 109 110 111 Degrees F.

Tables-Figures.xsx

Figure 7. Time/Temperature Relationship for Y-Nozzle Diffuser

-Plume Water Temperature (degrees F)

-Ambient Water Temperature Elapsed Plume Water Ambient Time Temperature Water (seconds)

(degrees F)

Temperature 0.0 115.0 86.4 6.3 111.1 86.4 8.1 99.3 86.4 10.8 96.8 86.4 14.2 95.1 86.4 18.0 93.8 86.4 22.4 92.9 86.4 121.0 116.0 111.0 106.0 C

3101.0 96.0 91.0 86.0 t

81.0 --

0.0 5.0 10.0 15.0 20.0 25.0 Elapsed Time in Seconds 1/6/2010 2:57 PM Figure-7.xlsx Figure 7

Figure 8. Thermal Plume Vertical Profile (96 degree F isotherm)

Existing 96 deg F Isotherm Centerline Proposed 96 Deg F Isotherm Centerline Sea Bottom for Multiport Diffuser

-Top of Existing Plume

-Top of Proposed Plume MLW (Mean Low Water) at Shallow End Bottom of Existing Plume

-Bottom of Proposed Plume 26 22 18 14

4.

+

4 4

4

4.

4 4

4 10 4-a

~

a -a-a-.

~-e

~

a 6

2

-2

-6

-10 0

2 4

6 8

10 12 Feet 14 16 18 20 22 24 1/6/2010 2:57 PM Figure 8.xlsx Figure 8

m M

M M

M m

m M m

mM

=

m M M

m-Figure 9. Thermal Plume Vertical Profile (96 degree F Isotherm) for Y-Nozzle Diffuser Proposed 96 deg F Isotherm Centerline -

Top of Proposed Plume Bottom of Proposed Plume Existing 96 deg F Isotherm Top of Existing Plume Bottom of Existing Plume Excavated Sea Bottom MLW (Mean Low Water)

Natural Sea Bottom 40 35 30 25 20 15 10 5

0

-5

-10 I1I Figure 9.xlsx Figure 9

APPENDIX A CALCULATION 16

ISUBJECT MULDIF'Run-Y-Nozzle with 135 ' F discharge temrnare A

,Job No: 7387685 Made by HAF Date 11/17/2009

,f6o dex Ret.

Checked SSH Sheet 1 of 2 A

PSL:Calc 016 Reviewed HAF Run the MULDIF model for both St Lucie diffusers assuming full flow and. a discharge temperature of i 150F.

The original calculations for the two diffuser runs duringthe uprate project were Calc 7 for the Y-Nozzle and Calc 8 for the multiport diffuser. This calculation is a revised version of Calc 7 for the Y-Nozzle diffuser at the discharge temperature of 1150 F.

Reference Drawings:

I 8770-G-664-1 for discharge diffuser profile 2 8770-G-66303 for pian view Composite of these drawings is attached as Figure 1.

From Figure 1, we see the Y-nozzle is actually a 450 nozzle With discharge centerline at 34 ft mlw.

From the unit I FES (see attached P. 1M1-9) we have the ports as 7.5 ft diameter and velocity equal to 13 fl/sec.

From Calc 7, we know that the 7.5 foot diameter is the inside diameter (ID):of each port, thus each port has an area of:

A itRA 2 = 3.14159 * (7.5/2) * (7.592) 44.18 square feet Using two ports at 44,1.8.sq ft each, assume the flow is evenly split:

From Calc 6, flow is 1,487 MGD for both Units I and 2; therefore each port has a flow of 1487/4 =

371.75 MGD

= 258,160 gpm

.Therefore, the discharge velocity = Q/A = 575/44.18-13.02 fl/sec

= 575 cfs We will use thenear-field model of Koh & Fan (MULDIF) for submerged multiport diffusers.

From MULDIF listing (Attached)

First Data card:

NC = 2 points defining one stratified layer DO-jet ID 7.5 feet UO = 13.02 ft/sec TO is discharge Temp = 11-5, from the proposal.

From Calc 7, we have Bookl.xls defining a curve fit of density of sea water as a function of temperature.

DENI

discharge density in g/cc at 115 degF,

1.016851 ThetaO = angle of discharge = 0' DJ = Depth of discharge = 34 ft SPACJ= Jet spacing, call it 115' (because jets are at 45' angle, make them far enough apart so they don't interfere with each other.)

Card 2 and.3: There are 2 cases of ambient depth and density, at the surface and near the bottom.

D depth= 34 and 0 TA = ambient temperature. Since AT =28.60 F., per Calc 6, TA 1=15 -28.6 =

864. degrees F.

Dena ambient density =1.023181461

Card 4 GRAVAC = 32.2 BLDR =

575 cfs RIVR = receiving water flow, =0 for slack tide /worst case

SUBJECT, MULDIF Run. Y-Nozzle with I I5 0 F dischiar I

Tabulate iry.Warksheet "lnutýPairameters-and'also save as. '"Y1.AT s oea x~i

Create blank output file Y 1..OT' Using these inputs and output filesý,run,,MULDiF.

Open output files in excelanid 'cle'ain :Up -sav'e as" Y l-.OUT xls and plot, centerline teminperature vertically.

Pl6t,on axis 'for ach of theY ports on Attachiiiefit 1 of Cac *7 Seeattac ent '1 for resuls.

,Next, comparethe results to the results,of Calc. 12, which w'as:p-r-ese'nted in the SCA for the following 3, cases:

-Pre,,-Uprte (Call6' Existinglp1*nt inCai 12) at ftll lo"ad an& Cw flow (AT *25 deg F, CW flow =

`575 cfs e pr 2

4 Uprated plant at fful load and CW flow (AT= -28.16 deg F; CW flow ='575 c fs, per port)

3. Upiated plait at fl 1 load but reduced 1CWflw6,(5:14`cfs per port) aind increased discharge temperature

-=117 degF (A=-32 deg F)

.Ifis seen,,that the results for the -new run, with respect.to AT, aremso-close to being thesame as Case 2, that they-are indistinguishable.

Thus the only change for te new run is the. increase inabsolute temperature. This is why the blue line on Attachment I overlies the

.green line, which represents Case 2.

Furth~ermorei, the new run is close enough.t0,be cnsidered i)dentical to Case 2 inISCA Figures5.1.1-land15.1.1-2. and themixig zone sizes specified:in SCA Secion5.1.1.2 for Case 2 also hold fordthenew run.:

With: respect to the mUltipo6rtdiffuser, lthesaimei result will:occur. Becausethe density,*differencte associated with the Mý§ialldabsolute

.temipera -ture change is so smallý the !resuilts for 'the thermal disharge at 115 deg F, for the multiport diffuser will betsame as SCA case 5, aind the mixinrg zone sizes specified inh CA-section 5-i...2: for Case :also hold for jhe new run.

'Therefore, the only difference,ýbetween thel 15 degree discharge,!cases. and the previous.Caseý 2 and, 5: (disch arge temperature at 113

deg F.) thermal plumaeshisthatthe absoluteitemperature will location along the.plume)&. This is bec"ause the ambient watef temperature has increased by 2 deg F. relative to the SCA cases.

m m

-m m

m m

m m U m

m m

MULDIF-Y-PoirtDiffUser parfamefte, Y-Port Units

,Deflnition Note NCI

.2 none Nimbir'of layers ASSumel2-layers at same~temp and density.

DO--

7.5.

Ft Jetcdiameter Discharge is through.

UO,ý 1'302 Ft/Sec

'Discharge.Velocity,'per jet Fr6m.CaIc 6.

TO

...,115.

Deg F DischargedTemperature From Conference call on 10/19:with Ron Hix DENI 1.01685096 g/cm3 Discharge density

-Calculated THETAO 0

none' Angledof discharge.With r*

ect to horizontal.

Two scenarios.-.

DI 34 Ft Depth of:discharge Depth of discharge SPAC 1-'15 Ft Spaing between let center-s Only 1 jet.:

D.

0 and 34 Ft Depth ofdischarge Depth of discharge, TA 86.4 Deg F Ambient River. temperature Dena-1.023181462 g/cm

.... Ambient: River-density,

GRAVAC 32.2 Ft/Sec2 Gravitationa constan Gravitational 'c0nstat BLDR 575 cfs Discha6ie&'flow Calculated RIVRI, '*.0 River flow ( Ofor slack tide)

Assume slackitide 1/5/0109Y4 PMCalc46'6-Mlsx'Input Parameters

m m*

m m

ml m

m m

m_

MULTIPORT SUBAQUEOUS DIFFUSEEIN AN ARBITRARLY` D YSTAT-IFIED ENVIRONMENT AA= 11 5.00 FEET A!,--A;A-....I A= 7.50: FEET, JET DISCHARGE ANGLE=

.00 DEGREES W/HORIZ JET'DISCHAkRGEV8`ELOCJ TY'=. 11"3'02,,FT/SECý JET DISCHARGE TEMPERAT. RE=-15.00 F JET DISCHARGE DENSITY= 1.016851 GRAM/CC JET DISCHARGE DEPTH= 34.00.FEET X

JET WIDTH DILUTION JET TEM JET DENS AM8 DEN AMBTEM

'DELTAT.

-,AALLOW T 46,84 "0.00016, 15.15771 1.0105i 111.0679 1.0 1772 1.02318 86.4

24.66787 17

.76.69625 1.'64824 28:194353 1.93673

,i99.27081 1.02033 1.02318 86.4 12.8708 17 91.45287 4.0785 35;64917 2.4'02'48

ý9 66.77561*

1.0088...

1,9023, 86.4 10.375601 17 105.9208 7.86018.8

42.0.8208 2.872831 95*i0769...

1.-02126 1.02318 t86.4 86769 17 119:9264 13.09831 48.12643 3.35084 "938391.....

1.02153

'1.02318 86.4 3.439t1 17 133.2993 19.78842 53.71106 3.83999

'921.8048 1.02174 1.02318

'86.4

'.446' 8

17.

145.9083 27.827471 58.83387 4,34372 9211,3868

1.02191 1.02318 86&4 5.73868 17 THIS IS FREESURFACE 1'213/29 11:63 AM;YI-u.~~xY1 Yl'ý6uf'ýý-Xlsx Y I

a.

FP SL Uprt Cacuto 7t C '616-iA dhl, T

Rho(actual) 30 64.25

.3.21 64.25'

40.

64.20 (50 64.17:

60, 64.:10:

70 64.02

ý80 63.95 86.4 90_

63,80

,95 96 97

.99

-1102 103' 104 105i 1.061t

<10,715__

108 1109 1127 3.....

...........8 1143 1145

116, 1117.,

118 119' Rho(est) 64,24201 64.2367 64.20901

64.1600' 64-0950 gleec

1.

029519 1.029434 1.028205 1.027163 6440140 1:.0025865 63.91701_1.024311 63.8465< 1.023181 63.804071.022500 63.7918

..0223005 63.7795, 1.022107

.63.7670 4`021907

.637543i 11,021704 63.7415. 1,021498 6337285 1,021290 63.7154i 1.021080 6837021 1.020867 63,6886i 1 020651 63.6t50 1.020433 63.6612 1.020212, 63.6473 1.

019988; 63.6332 1.019763 63,6189 1,0195304 6364,1.019303 63.5899 1.019069 63,57521 1.01,8833 63.15603 1.0185.94

'63.-5-452i 1.0'183.53 63.5300< 1.018109 63.5146 1.01,7863 63.4991 1.017613 63.4834~ 1.017362ý 63.46751 1.017108

~.63.4515< 1.:016.851 63.4353 1.-016592 6314190 1.016330 63.4025 1.016065 63.3858. 1.015798 63.3690: 1.015529

'1',2ýkQQ9 11:14 A

<12//209 1 :1:AMBook.

i;xlsx !,!nterpolate;

Cic. 16 Attachment 1 15 Degree F. Isotherm - Pre-Uprate Plant 15I~*

h 15 Degree F. Isotherm -

Uprated Plant with 117 Degree F.

Discharge Temperatu

m mm m

-m mm m -

mm mm m m

m m

Water Temperatures vs.Horizontal Center-Line Distance JET TEMP

-*-AMB TEMP 115 >4 110 105 !

100 95 9o.

85 80 0

20 40 60 80 Horizontal Distance In Feet 100 120 140 160 12/3/2009 11:43 AM Yl-outxlsx Center-Line Temperature

mm m

m m

m Jet Center-Line Profile and Jet Width (Feet)

Horizontal Distance 0

10 20 30 40 50 60 70 80 90 100 110 120 130 140 150 160 i-n 10 20 30

-40 so b

50

~60 f 70 800 90 100

-JET WIDTH

--4--Jet Center-Une Depth 4

110 O

Y'. DAT..

11.;0163'2918 34. 0 0.

32.2 2

7.5:

885.4 57,5.0O" 13.02 117.0

1.0 2280697

1. 02280697 0".

0..

34.

115.

Page,

FPLPI S IL Upra Ite Cluato C*6-106.6.7 30 3.2 Rh0(actual),.. Rho(esl 64.125'-..

40 50 60

'6420...

Si64.0i..

g/cc 64,2420 1.029519 64.23671 1.029434 64.2090 1.028990 64.1600 o1.028205 640.095'1.0271'63 64.01401; 1.025865 63.9170, 1.024311 63.8232 1i022807 63.8040': 1.022500 63.79181 1.022305 63.7795 !1.022107 70 80 88.4 90 91 92 64'.02' 63.8950 93

______63.7670!

1.021907

"_._94 63.7543., 1.021l704 95 63.7415 '1.021498' 96

.63.7285 1.02~1290, 97 63-7154; 1.021080 98 63.702141.020867 99 63.6886.1.020651 100 630 63.6750 11.020433 101~

V.

36 12 020212, 102i

.1.

_i 63.6473 1.019988 1.03, i.....

63,63321 1.019763

104,

.63.6189, 1,0195-34 1W05 6316045*

1.019303

.106!................

6.58991 1.019069 107 63.57524 1.018833 108_

63.5603: 1.018594 109i

.... 6.3.452 1.018353

.i......

63.5300:

1.018109 11161.5146' 1.017863 112 63.4991. 1.017613 113 1

63.4834i 1.017362

'114 63.4675, 1.017108

'115 63.4515jt1016851 116 63.4353F 1,016592

~117 63.4190 1.016330 11l8 6305 101606.5 S119 i 613.38581 1015798 120o 63.3690' 1.015529 A

'i111820099:29AM 9o" 1

Booki As lhtib IM&

NOT ES ON USING FORTRAN TQ UVSE, FORTRAN., THE. FO.LLIOWING PROCEDURES ARE NECESSARY

1.

PUTý YOUR., SOURCE PROGRAM' IN., USING THE PERSONAL EDITOR.

FOR EXAMPLE:,

A PROGRAM CALLED XXX SHOULD BE FILEDý AS. XXX.-FOR,1 7-THE. PROGRAM

'PDS HAS BEEN DONE THIS WAY. IF STARTING FROM:DSCRATCHi'B TYPD.:

i PE XXX.FOR tAND THEN TYPE 'IN YOUR PROGRAM. USE PE:.-HELtP, FO6R DIRECTION'S.

,ALWAYS SAVE, WITH THE NOTABS,,COMMAND!!! SAVE XXX. FOR NOTABS)

I BEý,FOREý YOU. QU.IT-PE._ USEý ESCAPE: KEY TO, CGO _FROM T EXT TO

COMMANDS 'AND BACK.

2.. ýWHEN'SOURCE IS,, READY; TO BE COMPILED,

ýAND, RUN, TYPE,:

I FORI: XXX MACHINE WILL-; RESPOND:

YOUObject FT'ename[XXX.BJ]:

.XXX*

ANDO OAjetWLEti BTHIT WILL. ASK YOUpp ALSO FOR Sourc~e ADbpc itng RESPONSE TO 1 3.WHEN DONE, IFt NO ERRORS,, TYPE:E PAS2: XXX IF YOU HAVE ERROR.S, Y",0 MUST GO 'BACK TO YOUR SOURCE' :CO'DE AND THEM. It IS, IN XXX.LST MHIEWILL.

TEILL -YOU.

TO PRýE.SS ETRKEY WHENý RýE.ADpY".

DO SO..

4.,WHEN: DONE.,

IF, NO ERRORS;,

TYPE:,

LINK, XXX IF YOU'ý 'HAVE ERRORS',

-YOU MUST GO,

'BACK TO.'.,YOUR SOURCE CODE* SAND'l FIX

,THEM. IT IS.IN XXX..LST MACHINE WiLL ASK YOU FO'R' Run File AND List File. ANSWER WITH':

XXX MACHINE WILL THEN ASK YOU FOR Libraries.

TYPE, IN FORTRAN. LIB 5.YOU ARE NNOW READY TO RUN ITHE.

,PROGRAM(XXX. EXEV)TYPE.ITS, NAME iAND ENTERi 'IT:

XXX-6.MACHINE W*IL ASK, FOR: FILE: NAMES, YOU.: SHOULD,. ALREADY HAVE CREATEDý SAN

I i

'~~INPuT: AND* OUTPUT :FILE FORi YOUR IPROGRM.,

FOR EXAMP:LE,*

F.OR PDS., !THEY

,iNPUT".DAT AND* *0UT~uIT.:DAT*.

T-YPE: IN YOUR*

FILJE*

NAMES AS', IT ASKS FOR*

THM I

WHNISDNY!'OTU ~L'BE.NYU EINTDOTU IE I

I I

I!

I-I I

m l,:

m m

MULTPOT$,

SUBAQUEOUS DIFFUSER' AY DITY STRATIFIE AA= I115.00 FEET I -- -- - ý I

A= 7.50 FEET JET DISCHARGE ANGLE

.0.,*0 EGEES W/HORIZ:l JETDISCHARGE VELOCITY= 1'302 F/*sEC i*,*****4*i,****

i JET DISCHARGE.TEMPERATURF= I i.00,F:

JET DISCHARGE DENSITY= 1.0 16330 GRAM,/CC JET DISCHARGE DEPTH'; 3.00 FET X

'Y JET WIDTH DILUTION JET TEM JET DENS, "AMiBDEN AMB rEM DELTA-T ALLOW., T 46.84 0.0001:6 15.A5771

.061051 I13.0679, 1.017221 1.02281.

88.,4.

24.66787.7 76.69324 1.686711 28.93918 L.93ý6,77 1101.2705,

1.

01989 1.02281

ý88.4 12.870,49 17 rl

)91.44051 4.17204.

35.63428 2.40267..

98'.7747'9 1...

r 102046*1. 1.02281 88.4 10.374*478 17 105.8867 8.03495, 42.04607 2.87337 97;07526 V.02084, 1.:02281.88.4 867526 17 1i;,985:3l 13.37625t 48.05749 3,35205 95"83643 1.021:12.

0228i

88.,

.2...

133.1668 20.I1004' 53.60047 3,44228 94*8876i

....... 1.,023:,1.02281 88.4.

4876

,45:6981:28.34249 58.67901 4.3475,7 9441,336 1.0215.1]

'1702281 88.4 5.7,336 1..

THIS IS FREE SURFACE 1I1!*/18/2009 9:595 AM Y

Y I :*o ut.xlsx Y 1I

m m

m PSL C 6

Center-Line of Thermal Plume Y-Port Diffuser Discharge Temperature = 117 0 F.

HoIzOntM Distance - Feet 0

20 40 60 80 100 120 140 160 0

Numbers in 94.1 Red are Ce-10 Temperature at Diamond in degrees F.

94.9 15 20~

1 95.8 25 92 30~

40 11/1&12009 10:05 AM YI-out.xlsx Centerline

m m

-m m m m m m m

m MULTIPORT SUBAQUEOUS DIFFUSER IN AN ARBITRARILY DENSITY STRATIFIED ENVIRONMENT AA= 115.00 FEET I -AA-I A= 7.50 FEET I

JET DISCHARGE ANGLE=

.00 DEGREES W/HORIZ

JET DISCHARGE VELOCITY= 13.02 FT/SEC JET DISCHARGE TEMPERATURE= 117.00 F JET DISCHARGE DENSITY= 1.016330 GRAM/CC JET DISCHARGE DEFPH-34.00 FEET X

Dth Y

JET WID'h DILUTION JET TEM JET DENS AMB DEN AMB TEM DELTA T ALLOW T 0

34 46.84 33.99984 0.00016 15.15771 1.01051 113.0679 1.01722 1.02281 88.4 24.66787 17 66.24353 32.90365 -1.09m 24.11517

!.6125M 105.40002 1.01896 1.02281 38.40000 17.00000 76.69324 32.3133 1.6867 28.93918 1.93677 101.2705 1.01989 1.02281 98.4 12.87049 17 91.44051 29.82796 4.17204 35.63428 2.40267 98.77479 1.02046 1.02281 88.4 10.37478 17 105.8867 25.96505 8.03495 42.04607 2.87337 97.07526 1.02084 1.02281 88.4 8.67526 17 119.8531 20.62375 13.37625 48.05749 3.35205 95.83643 1.02112 1.02281 88.4 7.43642 17 133.1661 13.81696 20.18304 53.60047 3.84228 94.88761 1.02134 1.02281 88.4 6.48761 17 145.6981 5.65751 28.342491 58.67901 4.34757 94.1336 1.02151 1.02281 88.4 5.7336 17 THIS IS FREE SURFACE Note : Valuh for 17 degree F isotherm interpolated linearly.

i i

"Listing of MUDIF!

I I.

I I

I i

I I

I

C MULTIPORT DIFFUSER" IN A. STABLY DENSITY-STRATIFIED" STAGNANT ENVIRN,..

C THIS PROGRAM WILL OUTPUT THE: JET:TEMPERATUREp DISTRIBUTIONAT A1/2 S

FT INTERVALS FROM TkHE JET ORiFICE-TO THE FREE SURFACE., INPUT C

PARAMETERS MAY BE -IN FPS,MKS OR CGS UNITS. WHEN SPECIFYING 'TABLE C

-6OF AMBIENT DEPTH, TEMPERATURE AND DENSITY, FIRST 'DEPTH MUST BE C

EQ~

RLESS THAN DJ,' THEN WORK TOWARDS SURFACE. lE, ýAMBIENT -IS, C

UNI'FORM, SPECIFY TWO POINTS, AT DJ AND AT 1 FT-WHEN THE.TWO C

VALUES"COINCIDE,AMBI'ENT IS.UNIFORM.

THE INPUT PARAMETERS..ARE C

DEFINED AS FOLLOWS:*

C NC NUMBER, OF 1ST"ATI'FIED LAY.E

,S I IN

.P1UT,T EDý C

DO, DIAMETERý OF INDIVIDUALý JETS.

,c U

VELOCITY OF JET DISCHARGE de TO'

,TEMPERATURE OF DISC'HARGE-C.

DENI.

DENSITY OF DISCHARGEI(MUST BE In GM/tCC)'

C THETAoC ANGLE OF DISCHARGE W/RESPECT TO HORIZ.

C DJ DEPTH OF DISCHARGE C

SPACJ JET SPACING(BETWESN CENTERS).

C D!fI=INC)

DEPTH AT WHICH AMBIENT SPECIFIED C

'TA(I=1,NC)

AMBIENT TEMPERATURE AT D(I'ý1,NC)

C DENA(I=1,NC) AMBIENT DENSITY:AT: D(I*=,NC.1) "").

C'

'GRAVAC.

GRAVITATI.ONAL, ACCELERATION PROGRAM MULDIF DIMENSION TA:50)

O),YT DIMENSION Y(6),YP(-6)

REAL LAMBDR, LAMBDS, M COMMON 'LAMB DR, LAMB DS,, M,'H, ALPHAR, ALPHAS, NC', ET, ED, PAI, GRAVAC, 'YT, 1K 1, ICHEKIQ,SPACJ I FORMAT(1I1O,7F10.6) 10 'FORMAT (3F10'.6) 11 ~FORMAT ('3F1'0.5)

'10.0 FORMAT:(Tll, 'MULTIP6aRT SUBAQUEIOUS DIFFUSER -IN AN ARBITRARILY. DENSITl "P1 STRATIFIED ENVIRONMENT~', I///T60,'AA=

', F6.2,' FEET',//T28,"1-----

2--AA ---- 1,T61,'A=-- 1,F6.2,1 FFE'/43/2,*-:-

3*

-,T160,'JET~ DISCHARGE ANGLE= ',F6.2,1 DEGREES W/HORIZ' T, 5T60,' JET DISCHARGE VELOCITYb-,,

,FT/SEC',/T55o I,/T11,

6 JET DISCHARGE TEMPERA 7TURE=6, F6.2,T F'DI

/TS6A,JET DISCZHARG6E D ITY=

EF/GRA/M/IcC, 8/5T6,'HJET DISCHARGE DEPTH=

'F6.2,'

SEETA///N 102 FORMAT (75HIROW BUOYANT JETS IN AN ARBITRARILY DENSITY' STRATIFIED ISTAGNANT ENVIRONMENT///5X,

.13HJET DIAMETER=,

FE6.3,.HMETERS-

.X, 223HJET DISCHARGE 'VEL

'OCITY=,liFE.2, 8HiMT.V/SEC/5X, 2,6HJET DISC'HARG,E.T 3EMPEPATURE=, 1F6.2:, 13HDEGREE CENTIG, 5X, 22HJET DISCHARGE DENSITY=,

41F10.7, 1IHGRAM PER ML/4X,18H JET DISCH..

.2GLE-l 2,8H DEGREES/

55X, 20HJET-DISCHARGE DEPTH=', 1F6.ý2 :6'HMETERS, 5Xi,l16HJET SP0ACING C-C=,

61F6.2, EHMETER'S) 103 FORMAT (75H1ROW BUOYANT JETS IN AN ARBITRARILY DENSITY STRATIFIED ISTAGNANT. ENVI;RONMENT,//-/5X, 13HJET. DIAMETER=, 1F6. 2,4fH CM.,5X, 223HJET DISCHARGE VELOCITY-ý/ IF6.2,8wIICM. /SEC/5X, 2'6HJET'bISC'HARGE T 3EMPERATURE=,1F6.2.,13H.DEG;REE CENTIG, 5X,22H-JET DISCHARGE DENSITY-,.

41F10.7, IIHGRAM PER ML/4X,i@H JET DISCH;.:ANGLE~i, 1F6.2,8H'DEGREEs/.

55x, 20HJET DISCHARGE 1DEPTH=~,1F6.2,4HCM,

.ý5X 16HJET'SPACING C I-C=,f 61F6.2, 411 cm.)

111 FORMAT (///7X,1HX. lOX,'HY',6X, 9H-IET'ýWIDTH,>3X, 8HD.I -L.1tft!6, 3XýýýA';7 T TE'M 1, 3XHJE~T DENS, 4X, 7HAMB ~DEN, 4X,7HAMBý jTEM, 4X, 7HDEiT.AT,,,3X,'7HALLOW T 120 ~

,(ýX FOMT'X53H 'INSUFF'ICIENT,,, DATA" ON: AMBIENT DENSIT'Y, N'`TMERT

ýý2 2'2 FbRMAT ('2Fl

. )5 J520 FQRMAT (iOX, 20HTRANSITION POINT TWO)

'532 FORMAT (1QX',2OHTHiIS IS' FREE SURFACE) 1222 FORMAT. (10X,2OH4TRANSITION POINT ONE)

'.204A READ(5T, 1) NC, DO, UO, TO,,.DEN i,.,THETAO,. DJ,ZSPACJ IF (DO) 2,~2,3 2GO TO 104 3READ(5,10) '(D(IX,TA(I},DENA(IYIlý-1,ýNC)

READ (,11)

GRAVAC,BLDR,RIVR TRA=(BLDR*TO+RIVR*TA(1)) /(BLDR+R~IVR')

PAI=3.,14 1592 65.

ALPHiAR=,. 06, ALPHAS=.16, LAMBDR=1 1:.l6 LAMBDS=I.

DO9999 I=1*;NC TH~ETA=THETAO ICHEK-0..

.C, CHECK~ PHYSICAL UNITS IF(GRAVAC-9OO4) 97,'

97, 98 9'7 (IF(GRAVAC-30.) 101, 99, 998 C.

IN FPS UNITS 9.9 WRITE (<6;IQ).sPACJ, DO,:THETAO",;VUOTO, DEN, DJ GO TO' 110 C,

IN MKS UNITS' J.011 WRITE (6,.02:)* DO,*UO,.TO, DENI,,THETAO, DJSPACJ' GO TO. 110 T N 'CGS UNITS:

98 WRITE

('6, 103) 'DO,:UO',{TO.', DENIF::THETAO, `JfSPACJ.

C TO 'FIND REFERENCE TEMPERATURE, AND DENSITY,ý IR=1

,IF< (DJ-D(IR:

112,113; 114 113.TRTA(,R.

DENR=DFNA (IR),,

GO TO 118 112 IR=IR+1 IF (DJ-D'(IR))

112, 113, 117 114 WRITE (6,1120)

GO TO, 20 4 117 SL=(DJ-D(iR))/(D(IR-1)-D(IR))

TR=TA (,IR) +SLt.(TA (IRý-1) -TA (IR) )

DENR-DENAJIR).4SL* (DENA*(IR-1)-ý'DENA(IPR)')

C INITAL CONDITIONS' 1188 Y(1y)*PAI PA DO* DO UO*o.05

,M= (1)*UO*05 MOLFJ=Y (1T)

,H=M*COS(THETA)

Y(2)=M*SIN(THETA)

Y(3)=Y'(1)*(DENR-DFN1) /DENR*0.,5 Y (4)=Y'( 1).s(TR-TO) ITR*'0.5

Y (5),46.2

DO*COS!(TH8ETA)'

ýy (6)=6.ý2DO**SIN (THETA)'

IK=2

'SQLAM= (1.+ýLAN.bDR*LANBDR) / (LAMB DR'*LAMBDR) 3 S-QRLAD=SQRT("

LAMBDS*LAMBDS) /LAMBDS C

TCALCULATION OF. DENSITY AND TEMPERATURED

RADENTS DO' 912 I

'DP1=YT(Il) -YT (I) 912 ED(I')=(DEiNA(I1)-~DENA(I)) /(DFNR-OPl) c CHOICEN OF INTEGRATION STEP

...... O/9.o.*

DS2'=DIJ/10.0'.

IF (WDS-DS2R) 2307,301p,.02 301. DS=DSl GO, TO '303 30t2 DS=DS2' C

INTEGRATION BY RUNGE-KUTTAM

.K~l 303 CALL RU NG S {SD S,6YYP,L).

301A Y20=Y(.2)

CALL' RUNGS (SDS', 6, Y,YP, L),

IF (S(2)*Y201,1 20,21,21

ý2,0 K=K+l IF(K- '3) 21','22,2.2:

22ý 'IF'(ICHEK~-l) 204:,-511,il204, 21J CONTINUE L OOP FOR TRANSITION POINT' iWO&

IF(ICH-EK-2)

'513, 514',204 513. IF(ICHEK-i) 203,206,206 203 TRANW=SPACJ C

ROUND JET 'SOLUTION

.51,4' IF Y(6v-DJ) 51,Y 531 531 WRITE:

652 GO TO 204 5301 IF ('IQ)~ 533,~533,2066 533 M=SQRT (H H +Y(2)

Y'(2))'

W IDTH=2, ~Y (1) / SQRT (PAf

'ýrM)

IF(WIDTH-TRANw) 2071,20,6, 206 C PRINT SPACING-CONT ROL

'207, S'JP--2,.*lD0 PI=IP*SJP I'F(S-PI)220,1221,ý2 21 220 ýGO TO 304

.22.1. IP=IP+l.

bENbTF=SQLAM*DENR*Y(3) /Y (1)

ýTDIF=SQLAM*TR*Y,.(4) / Y (1)

'DILU=Y (1)'/VOLFJ

,IF I (DENDIF)' 401,920, 920

'TDIF=~0.5

TDI'F C

TO FIND AMBIENT DENSITY AND 'TEMPERATURE VALUES

,920, IY,=2,

-9 06 IF F (Y(6.-YTIY):

90.0901,90.2 9Q01 DENAA=DENA,(I Y)

T*AG TA ( I90Y IY=IY+

GO TO 909 90'IY=IY-1 IF. (Y(6)-YT(IY) 900,90 1.,905 DENAA= SY Y* (DENAci Y)!-,DENA (I YY) +D~ENM IY-Y)"

GO TO.909, 902 IY=IY+1, GO TO 906

-909, TJ=TAA.-TDIF F

TDIFMý-TDIF TFI3-DILO) 428, 4'23, 423 428. IF(DILU-ZIP) 3,04,2545 425 ZIP=ZIP+.5 423 ALT-17.

WRITE (6,222) Y(5),Y,(6),ýWIDTH,;DILU,TJ,DENJ,'DENAA,TAA,TDIFMVIAT Go To 304 C

SLOT, JET SOLUTION C QHECK 'TRANSITION POINT ONE OR. ¶WO

ý20-62 I-E,F(Y(6)-DJ) ~522, 511,511'"

5

'ICHEK=ICHEK+I, IF, (ICHEK-2) 512,512,20 c

TRANSITION.POINT TWO, 512 S=SO Y(1)=Yil Y(:)

=.Y2

'y (3" 1-,

Y(5) =Y 5 Y(ý6~) Y6 I P=IPC IK=IKC IY=IYC' K=KI.

WRITE (6,520)

GO TO :303,

522 IQ*1 IF (ICHEK-1) 240,24.1,241 c

TRANSITION POINT ONE W'40 wRITE (6, 1222)

C STORE SOLUTIONS AS INITIAL CONDITIONS FOR TRANSITION POINT TWO SO*S Y2 Y* (2)

,Y3=Y('3)

,Y4=Y(4);

YS=Y(5),

TRANW2-~YAPHAS~PACJ/

I PI ALPHAP2)k IPC=IP" KI-=K IKC=IK.

ICHEK=ICHEK+.1-IyC=I-Y C

PRIFN SAN CONDROL

!211 PISIP*SJP IF (S-PI') 304,5-01,.501 501 I-P=IP+r N=SQRT(H*H+Y(2) *Y( 2 )}

WIDTH=Y,(1V*Y(1)/(SQRT(PAI) *M*SPAC-J,)*.2' DENDIMF=SQRLAM* DENR-Y(~3)/Y(l.)

TDIF=SPRLAM*TR*Y(4) /Y;(1)

DILU-Y (1) VOLFJ I* (DENDIED 402,906,906

'402 CONSTN0.5ESQRT(0AI,0.(5)

DENIF=oCONS TTDENI0F TDIF=CONSTl-TDrF GO TO,90,6 0

STOP END SUBROUTINE DERIVE (S,NY,YP)

DIMENSION Y(6)',YP(6)

DIMENSION ET (50),ED.A;50),YT(5'0)

.REAL LAMBDR,LAMBDS';M" COMMON LAMIBOR, LANBDS,.M,-H,'-ALPHA-R, LHi

~

C,~E, ARycXI 1, I-IEK, IQ,SPACJ Cb COMPUTATION OF DENSIT Y 'AND TEMPERATURE GR ADITENTS, AT Y 81'4 IF (Y(6)-YýT (1) ) ý8l,811, 812 812 IF (Y(6)-Y.TQK))

6806,813,813 805 EDD-ED (,)

ETT=ET(-I)

GO ~TO 70ý 8i3 EiDD=ED(NC-i)

ETT=IT(NC-I)

'GO. TO 70 066 IF (Y(6)-Y-T(IK))

8 0 0,80.1,80U2 8011 EDD- (ED,(IK)+4ED(IK-1) ) 0.5 FTT= (ET:( I-K)+ET'(IK-T) )':0:.'5 8 IK=IK+I1

,C-TO 7 0 800 IK=IK-1, IF(Y(6)-YT(IK))

800,801,805 805 EDD-ED (IK):

ETT=ET (J.K-)

-GO TO, 7,0 802 IK=IK+1, IF 1K-C)84A, 814, 807 807 WRITE (6,80.8) 80:8 FORMAT (10X,25H THIS IS :THE FREE SURFACE5):

RETURN

70 IF (IQ') 71i,1,72 C::

ROUND, JET :SOLUTION 71 ENTRAN=2..

A:R*...

kCLAM=~(l. +LAMBDRllLAMBDR)/2.

GO TO; 731

,C SLOT JET' SOLUTION T~2 ENTRAN=2'. *ýSQRT(2'. ) *ALPHAS?' SPACJ*m/Y(1 )J CLAM=SQRT'( l+A4D*AMBDS)/2.),

T3~ SQROT'M=SQRT~(Y(2) *Y(2),+H*H)

YP'( 1) ENTRAN

~YP(2)=CLA1ý

'GRAVAC - Y(1):*

Y(3)1/SQROTýM YP(3)=Y~l)

ROD,

Y2(2)/SQROTM

,YP(4)=Y~()

~ ETT Y(2)/SQRO.TM YP(5 )=HSQROTM YP(6V)=Y(2)/SQROTM RETURN-END 1SUBROUTINE RUNGS (X,H,NY, YPRIME, INDEX)'

DIMENSION Y ('7),,YPRIME'(74 ;-Z~(7-),Wl-(7), W2,( 7),W3('7),'W.4I

((1)

CRUNGS -

RUNGE-KUTTAi SOLUTION, 0F. SET OF FIRST ORDER 0.D4.E,.

FORTRAN' I:-

IF(INDEX) 5, 54

-1" DO -2. =1,N W1(I)=H *YPR-IME(I 2Z(T)=Y(I)+(Wl(I)*.5.)

A=X+I-12-.

'CALL DERIVE (-A, N,-Z,YPRIME)-

DO 3 I=l,N W2(I)=H

YPRIME(I)

A=X+H/2.

,CALL DERIVE (A, N, Z,,YPRIME)ý DO 4 T 1,Nl W3(l)-)H

YPRIME.(I);

A' -Z,(I)Y(I)

+W3 (1)

A=X+H.

CALL' DERIVE (A,N,Z,,YPRIME):

DO 7 Iý1,N~

V4 (I) =V

Y-PRIME (1)

CALL DERIVE.(X,ýN,Y,YPR:IME)

GO To, 6 5 CALL DERIVE (X,N,Y,YPRINME) 6 RETURN'

'END.

APPENDIX B CALCULATION 18

Golder A~ssociates ISUBJECT.

Isotherm Sizes'and PlumeqINineation-,

Jo jbNo. 09387,,687 Mai~*:H Fre'dianil, NDie'*

'6*630, 2009' IRef. FPL PSL tThermai d

Checked`

B H.Fsedian Ioa; k

S NfieNdt. e3 of 3

Assessment - Calc 18 ReiwdBH.Fdan

n.

Mixg Zone sizes A. Y-Nozzle From Calc 16, we have the proposed Y-nozzle plume-shown in spreadsheet Calc1 8.xlsx, worksheet "Y1"'

FromCalc 12,CCase2'w.. *,have lthe existing Y-nozzle plumihe shown ini.alc.18xlsx,,worksheet "*PSL-2' Firtt. clclate the centerlne' lume distanc&S~as'te siuareiro0t of thersum

~f the X;and Ycoirdihates' suarel"see.1st copy [e.g.1(2) andPSL2(2)]ofieach work e*

s t.heet Qnthe same heetf, nierpolate :the distances, etc..

torihe whole numbr,

absolute tempbe6aturesdowndto 96 degreesý F. Use ina6eainterpolatiofi:basd! oh,., A, For eachtemperature,* caluate the area of thbe cylin'der~enclosed bythaitis"Othenmiaassumin that the :Gausssian distributiorn used by the model to calculate Jet Width is four iines the standard devtin Asneape lo 1

,de frth prop~sed plume (w*6tkheet is called Y:1-i1 1~);

This'is t~th'si)lest case !bec e~iit s at *thb.e nterlire after~ only twebateps.i We assume a6tsiep,0 the ouietI from the ppe, haththe]jetwidthi s7.5 feeijthe6ipediajmeter.Atst`ep

1

' `46.84feet).

the jet Widthis -15.157714 feet :and th dinbr e rteil.teupe atrIe is 11.0679 degF, lATT ceitedine) = (111-*85)(11 10679-85) 0:

,0.997395-. Frorn-ihe Normal Distribution tab Ie (normal.pdf), 0.997395co~rre~sponds to about 0.07, sIt Iandard Ideviations,,

Therefore& the jetwidth out~to the 1111.degreF is0thbrm is (.07/4) *.(15 15771),=

0*f 35 f t

Usn h

verag end-area~nto

-oopt~h~oun.fotepipe pytl tto~h is tpw~a~

"(17!5*7*5/4)+(n*(3.0*3/4)/2)*~ 1036

From the firststptoteseconsep w84) 000601cuf Thus the total volume*within' the 111 degree isotherm is 103600601 cu ftk, or 1,036cu ft.

'Au'tomating the caiculai6on, seeworksheetY 1ti'1 1", Note that we add t'p0 b;,atSý 0, jetwidth-7.5 feet*a iand jet temperature = 11i15 deg"F. We will assume that the "top-hat" distribution of temperature holds at:stepl0: i.e. a'll oftIhe water isat the discharge temperature, so',all isothemrnsincludethe full jet widthwe see the actual calculated volume is-1,036.05 cubic feet.

The rest of the volumes have been calculated the same way for each temperature down to97 deg F. Volumes vs.. temperatures are 'summrarized in worksheet "Table 1 forthe propos dIdis'charge. From CaIc 16,,we notethat athe

,existing.discharge yolumes aretlthaesameias heproposed, except*theyiareshifted 2,deg F lower. Foibxample, the volume 6ofthe proposel* 1149deg isotherm is 1036.05, the volume for the existing 109 degF isotherm :is apoximateiy.the

!same. For our purse4here, we wilil"assume.that it is.,

Table 1 is also saved to a,,sierarate spreadsheet called Tables-Fig~ires~xlsx for p tng purposes.,

Golder Associates SUBJECT lisotherm :Size'salhd PlumeDeliiniation '

Job Noi 09387687 Made' B*y*H Frediani' Date; NoVeember,30j, 2009 Ref., FPL PSL Thermal' Ihekedl I S. Hoschek" Sheet

.2 of Assessment - Calc, 18 Rkeviewed'By Hk.'Frediani I

I..

I.I.I"I"

""I I

ý

ý,-

ý 1-1.Moxing ZoneSizes; B.-Multiport Diffuser The existing multiort diffUsO the6ral jplu 6was cIculatedi Calculation 13 as aSe'5. That out:tiS reprodUced here as' worksheet "PPSL-6*(

in spreadsheet Iac8 B.ixlsx In the first oPY,.of PSL-5(SAA), centerline, distance S is calculated. Un-needed columns are stripped out -Dilution je apd afribientfdensity, andallow T.Next, the whole numbrd abs6olte temre'ratures are interpolatedl hneaily, basedon deltaT,-

down to a jet iemperature.of94deg F. Then, voluiimeswere ca cua}ted on indiyiduali'emperaiur sheets as wasdone forthe Y-Nozz~le cas inAao;s spedsheet Calc18B'.'xlsx)ýforeisults.L

'Note for the existingcae, the upper tempra0ýt'ur'e limit is taken as "108"deg F, which isilthe first w'hole number temp~e'raiture" after the first step V*lumes:vs. temperatures are summarized in T6abe62. As wastihe case.for theY YNozzle, it is assumed thatt'h' proposed plukme"is the same" shailpae as*t*h"e existing, tbut2 dehle* F higdher at eachlocation.

Nexkt; comi'hbine th.eVnozzle and muti port results into one TbleaidF

2. Plume Delineatiorn A. Y-Nozzl*.

The plume is 66e delineated in viertibcal lj*P aJdin as wasA dn'e!in Cialculatio, 7h 'of the ýUpratebProject, ex.ce thtfit the 96 degree F isotherm width will be plotted instead of the distancelto the 17 degree F isotherm. First, the X values and the96 degreeF isotherm jet width from. worksheet"96" of calcl 8xlsx has been copied tb spreadsheet CalcI82A.xlsx.oon Worksheet 6. This represents the jet Width for the proposed discharge.

Next; copy. PS12 frLm2r Ca!tl68,xlsx to Caýlc182A xlsx as wehave *t calculate the

-egreejet'width for the existing case.

Do so using the same technique described for previous spreadsheets. Results'are in PSL-2 (2) and copied to worksheet6.

At~the farend of the piUme,6'add in slightly differentx' values for exis'ting plume wherebthe difference is greate rthanon*eh foot.

qCopy' the perinent, portioi table from worksheeht 6 to spreadsheet.6iledplurirUes in W h*ise~et'called Y-Noze[Oi 16!i missing values',an dcblcul6ate distaneto 96-degreeisotheti5_0ab6e(itive) and bew(regative) plume 'cnterline.

Golder

,Associates SUBJECT Isotherm ýSies' and.Plume Delineatio*n Job No: 09738687, Made By H. F`ediani Date:' November 30, 20,09.

Ref.' FPL.. PSL Thermal Checked:S. Hoschek 3shet of 3

Assessment - Calc 18 ReiwdB -. Fdin

.2. B.,MultiportDfusr Similar to A. on'sheet 2 thie existing multiport plume 96degree jet widthsaredopied from Calct8Bnxsxto worksheet 1 of

'Calc82A'.xisx. To determine the proposed 96-deree.jet widths, use the same procedure as'wa do**eforthe ekisting Y-nozzle. Start by moving PSLI-5(SAA)(2) from Calci 8B to Calc182A:xlsx and then add 2 degrees

,*pt0 qc jet temperature to convert to Proposed plme C~opy it~ again (3) and delete extra columns and~rovws then calculate. 96-degr~ee jet widths..

Pastetheminto sheet "I"andcopy tableto spreadsheetPlumesasworksheetiMultiport.

Pl0t the results.

Table 1 Y-N*Nz*eV6olume Encl6oed vs Temperature - Cubic Feet Temperature Pp

.s.ing1..13

'F:1.

(1 1 eg deg F

discharge)..

'discharge) 111 2,~1012.09 110

'2,1161 109 12,167.37 2,072.09 408:

2,.22 17.3 15.

2,146.10 07 12,297.77 2, 167.37

.06 2,380:63

!2,227.35 105 2,478.32

,,2,297.77 104 2,593.64 2;380.63 103 2,729.94

.2,478.32

,2.

1..

2,891.21

.2,59'3.64 101:

308226 2,7_29.94 100 X3308.90

'2,891.21 99 3,53.1 3,8.6

. 98 3,938.02

3308.90:

97 4,4419.08 93,583.19

.;96.i

":5,088.63" 3,938.02 12/3/2009 10:31 PM 12/3200 10:'1' PMTables-11gures.xlsx Table I

Figure 1. Y-Noule Enclosed Volumes vs. Water Temperatures

--*-Proposed (115 deg F discharge)

-6..--Existing (113 deg F discharge) 6,0o0 5,000 4,0004 3,000 1,00 94 96 96 100 102 104 106 108 110 112 Dqfprees F 12/3/2 10:31 PM 12/3/

10:1 PMTables-Figurcs.xL igure I It

Tbe 1. Multiport Voume Etncloscd~vs Temnperature -CbcFe Temperature -

0:

110

109 107:

106 105

104, 102 101

100, 99 98 97

96 95

94:

Proposed (115deg:F discharge)

,486.45.

501.25ý 518.75ý 539.48 593.46

ý628.46 670.27 720.34

780.43:

855.-12; l1,098;45' 1,34.6.

Existing (f13 deg F di*scharge) 473.88, 486.45.

501.25 5$1:75, 539.48 5ý64.12, 593.46

,6 28.4-6

670.27" 720.34

,855.12 957.13 1098.45 1304.36

M M M

M M

M m

M Figure 2. Multiport Enclosed Volumes vs. Water Temperature

-*-Proposed (115 deg F discharge)

--1-Existing (113 deg F discharge) 1,400 1,200 1o000 t 800' I

600~

400' 200 0 !

92 94 96 98 100 102 104 106 108 110 112 Degrees F 12/3/2, 10:31 PM Tables-Figures.xl.

igure 2

m m -

l

-m m

m Table 3. Coibined-Volume Enclos!0 vs Ternp"eata.

- Cubic Feet' p

erature-Proposed ExistingV Proposed

%Existing Temperate Existing Proposed Icre....

F *E~i Y-Nozzle Nozzle Multiport Multiport,

,F.

111i 1,036

.11 t

'0 I1!,i036 1,036 110 1,058

-, 8 110

0.

1,066 1,

11066 109 1,084 1,036 486 109 1,036 1,5770 534 108 1,114 1,058.

50

.8

.108 91,066 1615 549 107 1,149 J08.

519 486 107 1,570

,668 97 106 1,190

.1,1 539 501 106 1,615 1,730 115 1051,39 1,495~64 5

1.9 151,;668 1831,36 104 1,297 1,1190 593 5,39 104 1,730 1,89.0 160 103 1,365.

1,239 628 5641.

103 1803' 1,993 190 102 1,446 1,297.

6,70 53102 1,890 2,116 226:

I1N 1,541 1,365 720 628 101 1,993 2,261 268 100 1,654 1,446 780 67002162,339 99 1,792

.1,54,1

'.855 720 99

..2,261

'2,6467

".38-5, 98%

1,969, 1,654 957 780 98S,43 2,2 491 97 2,210 1,792

,098 855 97

.2,647 3308 661 96 2,544.

1,.69 1

,0957 96 2926" 3,849 9231 11ý3/20,09ý10:31PM 1able&&-igures.i Iable.,3

m m

m -

m m

Figure 3. Enclosed Volume vs. Water Temperature FPL St. Lucie Plant - Existirn

-41U-Proposed 4,500 4,000 3,500 3,000 1 2,500----

11000 I

So 02 94 96 98 100 102 104 106 108 110 112 DegresF.

-n m

m m

mm Figure 4. Increase in Enclosed Volumes Due to Proposed Increase In Maximum Discharge Temperature 1,100 -

1,000 900w 8w0 7W 4-6* 0 S 00 300 200W 100 96

-1 14 105 97 98 99 100 101 102 103 104 Degrees F.

106 107 108 109 110 111

mm m

=

m m

=

m x

46.84 47.01177, 49.S42,50 52.0734-54.60422, 57.13504 62.19k9 64.7275 67.258*72 69.78914 72.31996 74.8507.8 7 6.7 0 126, 78.2 97717 80.3386 84.2 1179 86.3879 90.12582 98.05875 98.24

.Proposed

!96 degree JET WIDTH 7.5 15.124 16.41 17.57 18.74 191.9 21.08 2'2.25 23.42 24.59 25'.75 2'6.92 28.09 28:.88 29,67 311.01, 3236 33:170 35.05 0

Prqpgsed 96 degre6JETý Eisting 96 deg'reejjeW WIDTH.

width Existinig,9'6 Poiiv Negative Y Positiv'e Y, N e"g'at i V 6"Y, degreejet coordinate co6edinate coor diate coordinate width 7.54 3.75

-37V.5,

-. 7 4.75239 7.58

-7.58 2.38

-2.38 4.78955 7.62

-7.62 1.39

--2.39 5.01972 8.20

-8.20 2.51

-2.!5 5.2176,6 8.79j

-8.79 2,6-1

-26'1 5.37907 9.37

-9.37 2.69

-2.69 5.49864 9.96

-9.96 12.75

-2.75 5.56963 10.54

-10.054 2.78

-2.78 S5.58329 11.12

-1'12 2.79

-2.79

,5.52789 11.71.

-11.71 26ý

-,2.76

ý5.38761 12.29

-12.29:

2.69-26 5.13632 12.88

-12.88 2.57

-2.257 4.73651 13.46

-13.46 2.37,

-2.37 4.1147314.05

-4.05 2.06020 3.773 14.44

-*14.44 1-.89,

-. 89 3.*48

14.84

-14.84 1.74, 1.74 3.19193 15.51

-15.51 1.66 0i6 1.60 16.18

-.1618 0.80-0.00000 16.85

-16.85 0.00 00 17.52

-17.52

ý19.29

-1,9.29 "0."00 b0.

12

/3/2 12/3/2\\10:31 PM' PI ý M6.xl,,ý.

U

m-m m

m---m m--

n--mmm m

u Positive Y coordinate

-m-- Negative Y coordinate

-4K-Positive Y coordinate Negative Y coordinate 25.00 Blue is proposed, Green is existing 20.00 15.00 10.00 5.00 0.00 0

-5.00

-10.00

-15.00

-20.00

-25.00 10..

12/3/.

10:34 100 120 Plumes.xlsx Y-k Ae Plot 6 PM

m m

=

m m

m

=

m m

=

m m

x 9.335319,

9.74419; 10,260g81, 11:2942?6 11.81095 12.32764 1,2.84433

13.36102 1'3.'87771 14:39440 14.9'11109 15.88063 17.0842,1 18.04317

.1,8.4081

'20.20402 21.15943' Exi stin g q&,'

deg jet

-width 1.47920 0.94234 0.97902 1.0o1959 1.ý05290 1.07790 1.09325 1.09721 1.68747 1.06076 1.01227 0.93421' 0.81216 0,75563 0.63299 0.00000 Existing 96 degjet width.

Proposed 96deg'jetmwidth

.Proposed Positive Y, NegativeY Positive-Y, Negative Y, 96 degjet coordinate coordinate, coordinate coordinate width L-48 0.74

-0.74 0.74

-0.74 1.052287 0.47:

-0.47 0.5*5)3.

,0.53 1.109.627 0.49'

-049 0.553

-O.55 1.1 56'54',3 0.51.

-05;0 058 20.58 1 9728.1 0.53ý

-0.53

.0.*60

-0.60 1.23) 1172 0.54

-0.54

.0.62

-0.62) 1i257261

-0.55 055 0.63

-0.63 1.274399 0.55

-0.5 70S5 6.64

-0,64 1.2811:J3-0.54

-0.54

.0.64

-0.64 1.275561 0.531

-.0.53 0.64,

-0.64 1.255149 0.51 0.51:

0.63

-0.63 1.2r63'3 0.46

-0.47 0ý.0461

-0:61 1.1227,05

.0.41,

-0.4 1

,.0.6

-0.56 1.1499712 0.' 38,

-0.38 0.57

0.57

1. 150631 0.32

-0. 32

0. 5

-_0.58 1.02 1857 0.0 0.00 0.51

-0.51

ý0.82474.7 0Q.411

-0.4 1 0,84 172 04 2

-0.42 0

0'.0..00"

ý0:.00 12/3/2ý 10.32 PM 12/3/2 0:32 PMPfiumes!ýX'sK',tio

--*-Positive Y coordinate

-*-Negative Y coordinate

-s-Positive Y coordinate -

Negative Y coordinate 1.00 T-0.80 0.60 0.40 0.20 0.00

-0.20

-0.40

-0.60r

-0.80 T Blue is proposed, Green is existing 5

10 25 is

-1.00 1/5/2010 11:19 PM PIumes.xIsx Multiport Plot

m m

,MULTIPRi>fSUBAQUEOUS DIFFUSER'IN AN ARBITRARILY DENSITY STkATIFIED ENVIRONMT AA=- 115.00 FEET

.A= 7.50 FEET, JET DICHARGE ANLE=

.00DEGREES W/HORiZ, JET DISCHARGE VELOCITY=ý 13.02 FT/SEC

- .JET>DISCHARGE TEMPERATURE=, 15.00aF JET DISCHARGE DENSITY= 1.016851AM JET DISCHARGE DEPTH=, 34.,00 FEET S

x 46284 0

'76.69625

-.1 105.9208

`7 119.9264 13 133.2993 19 145.9083 27 THISJ1 FREE-SURF

AMB' JET WIDTH ýDILUTION JET TEM JET DENS

MB AMB TEM DELTA T

).00016 15.15771, 1.01051:

F11.0679 1.017,72 1023 86.4 24.66787

.64824 28.943531 1.93673 99.27081 1".020335 t.0232:

86.A 12.8708

.0785 35:.640917 2.40248" -96.77561

."02 0818 102ý32.

8A 10.37561

.86018 4.2 208208 2.872183 95.0769 1.021261 1.0232 86A 8.6769

..09831 48.12643 3.35684 93.8391 1.02153 1.0232 86.4 7.43911

.78842.

53.71106 3.83999 92.89148 1.02174 1.0232 86.4 6.49148

.82747; 58.83387 4.34372 92.13868 1.02191 L.0232 86.4 5.73868 ALLOW T

17 1~7 1,7 17 17

'ACE I.-I 12/3/2t~

3:40 PM ac

.IxY Cýi

FPLý P'-,.11~

ULTIPOP BAQUEOUS [ FUSERR INA' An ARBTARIL DENSITY S TRATIFIED' El tVIRONMENT 00 FEET:

1--.

AA ----

-41 A= 7.

5o0 FEET" I

i JETbDIS'CI-;

HARGE ANGI.00.DEG

-REES W/HOFtIZ JET'DISC:

HARGEVELOTY-13029

'FTSEC, 4*

- - - - ~Ic*'*

JET DISC JETODISC JET DISC HARGE&TEMP ATU RE=* 13. 00.F

.HARGE DENS Y= I1.017362. "'GRAM/CC

HARGE DEPT 34.00 PEE T

x Y

46.84: 0.000 15 65.32 79',~ 0.9796.

76.70 13 )

1.58214 91.4735' 3.91752, 10i5.978 7.55859 120.05, 12.6169 1331524'- 19.1019 146.266 26.9274' THIS IS FREE JET WIDTH DILUTION. JET'TEMý

2'3~.69739966, 28,9508:

35..67405 42.141262 48.2433 53.90034,

.59.10154 SURFACE 2.40216 2.87192 3.34881 3.83613 4.33722 109.1Q

'95. 15929

'93.49754 92.28745 9.1.136169

'06."62'671 JET DENS 1.-01,82 1.0210723, 1.02159 1.02186 1.0.220.6 1.0 2 ý 222

'AMB DEN 1.02344' 1.,0'23,44:

1.02344

,1.023,44, AMI TEM.DELTA Tý 85~ ~24.15036 S 17' 985 85, 85 85 85 12.60128 10.1593 S8.497*54*

7.28745 6.361691 5.62671 ALLOWTfi7.

1:7 17 17 17 1-7 17 12/3/?7-'9 8:41 PM Cli8~~ S-Cl.alilc 18. x k x PSL-2,

MULTIPORT SUBAQUEOUS DIFFUSER IN AN ARB*I TRARILY DENSITY STRATLIE D, ENVIRONMENT AA= 115.00 FEET AA---I A= 7.50 FEET JET DISCHARGE ANGLE=

00 DEGREES WfHORIZ JET'DISCHARGE VELOCITY= I 3.02F`T/SEC-

- ~*******~I5*********************JET DISCHARGE TEMPERATURE=1 1.00 JET DISCHARGEDEN:T-"Y= 1.016851 GRAM/cc JETDISCHARGE DEPTH--- 34.00, EET ALLOW S

X Y

JET:WIDTH DILUTIOIN JET TEM JET DENSI AM'BDEN AMB TEM DELTA' T

46.84 46.84 0,00016 1 5.1577.1.:

1.0.1051 111.0679 1.011772 1'.023,181 86'.4 24.466787 17 47.01 47.01 0.01 15.24' :_

1.02 111 1..01:774 1.02318 86.4

'24.6 49.54 49.54 0.155 16.41i__: "

09 110 1.01796' 1023318

.86:4 23.6 52.08 52.07 0.29 17.57 1__._..

117 109 1.01818 1.02318 86.4 22.6 54.61 54.*60 0.43, 18.74 1.25 108 1:.01840, 1.02318 816.4 i21.6

.57.14

.57.14 0.57 19.91 1.33 107 1.01862 1.02318 86A

.20.61

.59.67 59.67 0.71 21:08.

1.41 106 1.01884 102318 86.4 1,96_

62.21 62.20 0.85 22.25 1.49 105 1.01906 1.02318 "86.4 18.6

,64.74 p4,73

'.0.99 23.42 1.57 04

1.01928 1

ý023 18

86.4 17.6__:

67.27 67.26 113.

.24.5.9-1.64 103 1.1.950 1.02318 86.4

.16.6;"61

.69.80 69.'79 1.27 25.75 1.72

'102 1.01.973 1.023,1'8 86.14 1"5.6 742.34

.72-32 1,411:

26.92, 1.80

101,

.i 01 995....... t.0231 "

864, 146.6,

1+-

174.87 74.85 1.55 2809

1.88 100 1.020173 1".602318 86.4 1361 176.73959,76.69625 1.64824

28294353, 693f73 '.-99'.27081

.02033

1.

02318

864 12.8708.

1 78.32'

-78.30

.91-

29.67 1.99 9 :' 1.02039 1023*18 86.4 1-2.6

.84.27 84.21 2.89

.32.36

. '217 98 1.402061 1L02-318 86.4 1.1.6

'90.21 90,13' 3.86 35.05 2.36 97

'1.02086 3

1. 0231'8

,86.4 10.6 91.543769 91.45287 4.0785 35.64917 2.40248 '_96.77561 1.02088 1.,02318 86.4 *10:375611.1

'17

.98:24

.98.06

.5.81 38.$519 2..

262 96 1

.02105 1.02318 86.4 9..6, J 06.21204' 120.639>5&

134.7601 148.53821 105.'9208&

'1 19.9264 133.2993 145.9083

'786018'

'1:3.09831 19.78842 27.82747 42.08208-4 8.12643:

,53,71106:

58.,83387 2.87283 3.35084

1383999, 4.34372 "95.0769*

93.839F1 92.89.148,

,9213868

1,.02 126-S.02 153 1.02174 1.0219,1 1.023,18 1.02318 L02318 86.4

86.4 86.4

,86.4 8&6769.

7.43911 6.49141388 5.73868, 317'

'17 17 THIS IS FREE SURFACE 12/3/20 '

42 PM C~1.~"' 2 calc 18,;

N' 1 (2)

m m

f,FPL PSL UpraL~

C~Ac, 121 M:

'ULTIIPO1BAiQUEOU FUJSER:IN ARBITRAR DENSITY S TRATIFIEDVIRONMENT A:A-I5

00OFEET A= 7.

50 FEET "I

AA I.I1 JETFDISC HARGEANE.00IDEC REES EIZ JET'DISC 'HARGEVEiTY=' 1302 [Fr/SEC:

- ~~*JET DISC HARGE TEP ATURE= I 1 00 F JET DISC I ARGE.,DEI Y= [0 17362 GRAM/CC JET DISC

,HARGE DEJ 34.00 FEE TF AMB AL W

JET" IDILUTION JET I*EM JETUDENS! AMB DEN. AE ALLOW WIDTH TEN DELTA.T T

4,84 46.84 0:00015 15.15771 1.01051 109.1i504 f:0182

.0234 85 24,150361 i7 47.23 47.23 0.0. 2 1:5.34 1.02 109 1.01823 102344 85 24 "

49.82 49,81

.0.16 16.53 1.10 108

1.01845 1:,.;02344 8

.5 23 52.40 52.40 1.'0.29 17:73 1.18 107.

1.018671 f602344 85 22 54.99 :54.99

'0143 18.92 1.26 1,06_

1.088 1.!02344 85 21""'."21' 57!58 57.57

'0571 "

20.11 1.34 105 1.01910 I102344 85

-'20 60.16

'60.16

,0.71 2131 1.42 104:

'1.01931 1.02344 85

-19 _

62.75

6. 2.74 "0.84 22.50 1.50 103 1.01953 1.02344

.___ 85 18, 165.33529 665.3279 0*979604 23.6974 1.58 102 I?.01975 L.02344 85 17 67.93 67.91 "112 24.89 1.66

-106V 096

.24 85

'6____

70:51 70.50 1.:25 26.09 1,74.

100

'1.020168

1.

02344 85 151___

"73. 10 73108 1.39 27128 1.82 99 1.02040.

102344 85 14

'75.69.

75.67 L.53 28.47 1.90

.98 110206i L.02344.

85

- 13

'76.71758 >76.7013.'T:.!58214, 28.9508 1:93665 97.60127,;

1f.0207 1.02344.

85 12:.6012 1.7.

S80:37 80.34

.2.16 30.61 2.05 97 1 02083 1.02344 85 12 F -86:,45 86.39 3-*31 33:36 2.24 1

.96j:

1.02105 1i.02343 85 411

_51_

1 91.55738, '91.4735

3.9.1,752 35.67405 106.2471, 105.978 57.558559 42.14262 1,20.711ý 1.20.05 1261691 48.,2433 134:18831t 133.524 '19.*0197 2 53.90034 148.7244 146.266 26:192742 59.10154

'-THIS ISF.REE SURFACE 2.40216': 95.15929 1 02123 2.87192t1 93,49754:

1.0215ý 3034881 92.28745 1.ý021896' 3.83613,

.91.36169:

.1.02206 4.33722

90.6267.1 11.02222 1.02344 I.02344; 1.02344 1.02344, 1.02344 85 85 85 85.:

10.15931 8:954 7..28745

'56.36169 5:,62671 17 17

'7

.17 12/3/20(vý VA2 PM PCaIcI8.xl-'-PSL,-2 (2)1'

Bm m

m m

-I m

MULTIPORT SUBAQUEOUS DIFFUSERIN AN. AR*BiTRLYlDENSITY$ ST TRATIFIED ENVIRONME9NT AA= I 15.00TFEET I----AA- -.-- I A= '7.50 FEET A

4ý*

JET DISCHARGE

'ANGLE=

.00DEGREES W/H6RIZ JET DISCHARGE VELOCITY-13'.02LFT/SEC JET DISCHARGE TEMPERATURE= 115.00 F JET DISCHARGE DENSITY= I1...16851 GRAM/CC JET. DISCHARGE DEPTHIý 314.00 FEET Tota IJJET Et TE AT(6t standard 111 d~eg JetEdAra Vlm S*

~

~~WIDTH C1

N L: E);

devi.ationts, : width.,

i:

0 0

0 7.5 115 7.5 44.178609

46.84 46..84'..

0.00016 15.15771 fI 1.0679 0.;9973953 " 0.0722242 0.273687 0.0588297

'036.041

47. 01 47.01 0.011'

11.

1

.. O00"0000'00.0000

0 0.005055;

...5

.:1 1

Total Volume=

1.036.05 cuw.feet metem.p,

85.00 deg F.

temperature of calculationi=

'111.00 Adeg F.

12/34,

4. 4 3 P Mlý 12/3/.

8:3 PMCalcl8.*

Yl 111l

.d

m m

- m m

m

- m m

iMULTIPORT~ SUBAQUEOUS DIFFUSER I -A*NARBITRAikRILY DENSITY STRATIFIED ENVIRONMENT AA=- 115.00 FEET A= 7.50 FEET JET DISCHARGE ANGLE=,.00:DEGREES!,Wi'wHORIZ,'

JET DISCHARGE VELOCITY¥ 13.02 FT/SEC JETDISCHARGETEEMPERATURE*=: l1:5.00*}F JET DISCHARGE DENSITY= 1.016851 GRAM/CC.

JET-DISCHARGE O.EPTHý 34.0.0 FEET To~tal JET 6T/

(AT. "andard I I0degjet En.Aea Voum Sý x Y

JET TP-M AT/i (rdT Noande WIDTH CL) deviations widti 0

0

0.

7.5 15 7.5 44.1,78609 46.84 46.84-0.00016 15.157711. H111.06*79 0.9590339 '-0.289236*:=":

1-.096040 0.9435015

[056*.76 47,011 47.0-1*.

0A0:i1 15.241 iAi

10.96153851 0.280074,4:

1.066873 0.893954:

0.179 49.541 49.541:,

0.15 16.41 1106;

1 -

0.000000%] 0.000000

,0 1131889 Total V* I,

1. 058.05 61ik

rnbient 1telbfniý=

ý85.00 degF.

temperatureofcalcuiation 1 10.00 deg F.

12-/') 8:43 PM (f

yl -110,

1týa109'JI,

.ý -. 1'.

mmi m

m m

MUTIPOR T SUBAQUEOUS DIFFUSERIN)NN ARBITRA IENSITYSTRATtFI ED-EN IONMENT AA=.115.00"FEET AA,-,--t "A=

7.50 FEET

,JET DISCHARGE&ANGLE=

.00 DEGREES&W/HORIZ JET DISCHARQE YELOCITY 013.82,lTR/SEC JET DI'SCHA-RGE TEMPERATURE= 115.00 F JET DI.SCHARGE,,DENSITY= 1.016851 GRAM/CC JET'DISCHARGE DEPTH= 34.00 FEET XIDTH y

ETT s

re End ArEea.

Volume.

WIDTH JET JE'.'EM CL)ý deviations w-idth4.178609 i

0 "....

0 7.5

1.

5 7.5__

4 4.178609 46.8 4 4 6.8 4 0~.~0 00....

1.1 1..0 6 7 9 0.9 2 0 6 7 2 6 004 0 6 5 73,1

.54 6 9 1.8 6 4 2 9 2 3 10 7 8.3 2 5 47.01 47.01 010&1 15.24 Ill 0.9230769 0.400107 1.524109

.I.8244059*

0.3 316986 49.541:

49-541:

0.15 16.41 110-0.96 -

0.285734, 11719910,% 1.0786438 3.6755726 52.08 52.0,7.

O;

-0.29 17.571

'109 1

6.000,00 0.00.0000 0

1.365536 T'taa Vo.l'umle =

I-,083.68 cu feet ambient temp 85.00 degF.

temperature of~aleulation 109.00:

,ge, 12(/-120

-.44,PM ac8xl 0

Cal'cl'8.xt.

I 109.

-m m

m m

m1 m

m MULTIPORT SUB3AQUEOUS DIFFUSER IN AN ARBI*TRARILYýENSITYSTATIFiEDENVIRONM'ENT' AA= 115,00 FEET I

A= 7.50 FEET JET DISCHARGE ANGLE&=

.-00DEGREES W/HORJIZ JET DISCHARGE VELOCITY= 13.02'FT/SEC E

JET DISCHA ENIRG E TEM0PERATURE7'8 115.00 F JET DISCHARGE DENSITY=-* E01 6851 GRAM/CC JET DISCHARGE DEPTH= '34.0,0 FEET

__tal JET J

TEM AT/

(AT standard 108 degjet EdArea Volume ID TH.CL) devaions width 0

0 0

7.5 1715,5 4178609 7

ii 5

44 i. 178

. &..646.84 0.009016 15.1.5771 11.H0679 '0.8823112 0.5,00421 1.896308 2.822772 A 100.80,8

. 70:1 47.01 0.01 15.24 1

0.8846154 0.95181 4

".886273 294463i t0448282 9.5.

49.541 0.15 16:41

110 0.92 0.408367 1.674875" 2.203201

.6S32783

'52.08

.52.07.

0.291 17.57 109`

0.9583333 0.291752 1.28182,6,,

1.2904686 4,.423545 54.61 54.601 0.4s 1874:...

1f08 1

0.000000 0.000000 6 1 0;-:0

1..63394 Total

,olum.e

=

1, 13..68 9 cu feet aben tM'P

`85.00 degF.

te~mperature of calculation,=

%108.00.

deg F.

12/3/ý 8:44 PM

Calc 18.

yl 108:

m m

mm m

m MUL-TIPORT SUBAQUEOUS DIFFUSER IN AN ARBITRARILY' DESITY STRATIFIED EIN NT' AA= 1! 5.006FEET

.I--:--AA----- I-A=

7.50FEET

..* JET DISCHARGE: ANGLE=

.00 DEGREES WHORIZe JET DISCHARGE'VELOCITY= 13.02'FT/SEC JET.DISCHARGET*E*MPAT URE*= l1$.1Fb JET DISCHARGE DENSITY= 1.016851 GRAM/CC JET DISCHARGE DEPTH-34.00 FEET DTotalHET AT/

(4T standard 1

degiet End Area Vol"me VITotlJT JE L

deviations widtw 0

0 0

7.5 11

.5 44 1780 46.84 46.84 0.00016 15.1577:1 111.0679 0o.8439498 :0.582516

?2"1207401 3.826941f8 1124.29 47.01 47.01 0.001 15.24 111 0.8461538 0.578021 2.201829 3.807648 0.656073 49.54 49.54 0.15 16:;41 110

-0.88

0.505635

.2.073812 3.3.7717546 9.09787 52.08 52.07 0.29 17-:57 109F 0.9166667

.417160 1.832813 2.6383098

. 7.617301 54.61 5.4.60"

,0:43 1.8174 08 0.9565217 0:298167

£9711.8.1.533.077 5.281606 57.14 57.141 0.7517 A1.91 0

1 0..000000 0:

.0 00000 0

1.941084 Total Volume:

1,148.88.1 c:fufeet amfbien.t` etemp

85.00 deg F.

temperature. of calculation =

d107.00

!degF.

12/3I~

8:44 PM CaIcl8.I YI 107

,Qale 18..-

Y. L 167'

m m

N m

m m m m m m m

m m

MULTIPORT SUBAQUEOUS DIFFUSERIN" AN ARBITRARILY DENSITY STRATIFIEDENIRONMENT""

AA=..] 15..00 FEET

'A=

7.5,0 FEET JET DISCHARGE:ANGLE-,

.00 DEGREES, W/HORIZ JET DISCHARG1E VELOCITY-13'.02FT/SEC.

-JET DISCHARGE TEMPERATURE=

.15.001F JET DISCHARGE DENSITfY-1".01'.685.51.GRAM/CC, JET DISC HARGE I EPT.

34.0FEET DtHJE.T/

(AT statnard 106 degj*j.

EndtArea

.Voume VIDTHotl JT JE TM CL) deviations width 00

.511Is,___

7.5 44.178609ý 46.84 46.84.

0.000.16 15.15771 ri

,110679,'

0.8055885 o.65754 2

491716-4.8762585 1.148.865

,47.01 47.01 0.01 15.24 1"

0.8076923 :0.653566' '2:.489599 4.8679743 0.837364

'49.54 49.54

.0.15 16.41 0

1 0:84 0.590514 "2.421934 4:.6069578 11.99678 52-08 52.07

0.29

.17.57 109 0.875 0.51I'6781.2.270502 4.0488634 10.95966 54.61 54.60 0.431 18.74 108

0.91,30-435 0.426548 1.998674, 3.1374251 9.098992 57.14 57.1 0.57 19.91 107

.9545455 0.305025 1.518362 1.81.06747 6.265087 59.67 59.67 0.71 21.081 106 1

0.000001, 0.000000 0

2.2926041 Total Volume 19.2 cufeet

'mbient ternip,:F

'85.00.

deg.F:

t11emperaturel eo calculation =

106.0.0 deguT

'1213/24,.,.

!ý8:45.:]?M, Calc'i8.iý

¥YI 106

MULTIPORT SUBAQUEOUS DIFFUSER IN AN ARBITRARILY D-ENSITY 'STRATIFIED,ENVIRON4MENT AA= 115.0. FEET A--- --- 1 A=.7.5.0 FEET.

JET DISCHARGE ANGLE.

.00:DEGRES W/HOiiz)

,i*

,:i~ !,;i*:**

- ***** ***i JET DISCHARGE VELOCITY=

3J1.02T*F/.SEC JET DISCHARGE TE:MPERATURE= 1 15:00.E JET DISCHARGE DENSITY-.iE.0 16851 GRAM/CC JET.DISCHARGE DEPiH= 3.:00 FEET Total JET JE TM [T!

(Vstandardo 105 aegiet ndd re Volume

_W IDTH.

Cl.::L) deyiations

-w idth 0

0 0

7.5 11 5 7.5 44.178609 46.84 46.8 0.00016 15.1577-111.0679 U0.7672271 :0.727973, 2.75860l 5.9767811i 1174,639 47.01 4 4701 0.01 151.24 ill 0.7692308 0.724381 2.759354 5,9800439 1.027501 49.54 49.54

0.15 6.416".

110 0.8 0.668047 2.739929 5.8961454 15.03716, 52.08 52.07 0.29 117517 109 0.8333333 0.603857 2.653073 5.5282511 14.46512ý 54.61 54.60 0.43 18.7N 108 0.8695652 0.528700 2.477325 4.8200952 13.10266 57.141 57.14 0ý57, 19:91 1L07

.0.90909091 0.436601 1 2.173327 3.7097091 10.80011,

.6.59.67 071 21.08 106 0.952381 0.312379 1,.6462291 2.12i848.1 7.392083 62.211 62.20 0.85 22.25 105 1O

.0.000000 0.0000000 0

2.694998 Total VoIume~

1,239.16

&cu feet amibient t& mp =

85.00 deg F, u~mperature of dalculation6, t105.00

-deg,,F.,

12/3/2(

8:45:PM Ck8x 10 Calc]8,xý 11,105,

m Nm m

m m

m MULTIPORTASUBAQUEOUS DIFFUSEREINEAN ARBITRARILYDE EDE AA=, 115.00 FEET,

-A----1 A= 7.50 FEET A'*****

JET DISCHARGE ANGLE=

..0,0 DEGREES,.W/H*ORIz JET DISCHA;*RGEVEELOCITY=

P**!3.2:FT/SECý

,,, *JET DISCHARGE TEMPERATURE= 1 15;00: F JET DISCHARGE.DENSITY= 1.0 16851. GRANM/CC JET DISCHARGE DEPTH= 3*4*.

00 FEETl WIDTl J

.,T!

(AT/

tandard 0.4.dg jet. E Area Volume.

.Total JET JETTEM CL deviations..widthl 0 :

0.

0

ý7.5 115

]

__44.17:860__

9 46.84 4..*841 0.000116 15.15771 1-11.069 0.7288658 0.795318 3013801 7.133765

'1201-736 47.01 47..011 0.01 15.24 IIIj 0,7307692 0.792032 3.03 17/0553) 7.1491ý67i.-1.22ý7394 49.54 49.54.

0.15 5.

16.41 f 10 0.76

.0.740860 3 8 7.25 14735 18.23352 52.08.-

52.07.1 0.29 17.517 109

.07916667.

0.683542, j003*173 7.083534.

5

.37 8.15042 546.

"54,606

.0.43 18.74 108 0.860,890.618151 "2.896463' 6.5890929 1 7.31-1,74 57.14 57.4I

.0.57 19.91 107 0.8636364 0.541'486 1.695428 5.7061717 15.56777 59.67 )59.67

.,0.71 21.08 10,6 0.9047619 0.447400:

2.357790 4.3661617 12.75319 62.21 62.20: "

.0.a85 22.25 W5

.0.95 0,320291 L.781501.

2.492652 8.684356 L

64.74 64.73

.99 M

23:.42[

104 0.00000 00*

00000 0

3A156097

Total Vo1lune =

1,29 6.82 cu feet ambient temp =

,85.00 degF.

'tempeirature of calculation i =

104.00 ideg F.

12/3/2 8" ý::PMý 123/,

ASMCalcl.8.{

Y1 1:0 4.

11

m m

m

.MUtLTIPOR-T ýS.UBAQUEOUS DIFFUSER IN iqAN.

ARIRARILY DEST0TRTFE E

IR NMN AA= 115.00 FEET I--- AA---I A=: 7.50 FEET JET DISCHARGE ANGLE=: -.0O'DEGREES W/HORIZ JET DISCHARGENVELOCITY-13.02 FT/SEC

- - *:****;Ic**

JET DISCHARGE TEMPERATURE= 115.00 F JET DISCHARGE DENSITY¥=. 1.016,851 GRAM/CC, JET DISCHARGE DEPTH= 34.00QFEET T6tal JET JET (EMAT/

(*T standrd:

103 deg jet JE TEEnd Area.

VO eV,lue SYWIDTH

_E*_

T

)CL) deviations width 0,

0 0

7.5-

115, 725 : " 4.178609

-.46.84 46..84.

0000016 15.157741:

.11.0679,: "0:6905044 0.8606.19.'

3,261255":.,83533183.123'0.298 0"

47.01

.00 15.24" 11 0.6923077 0.85,7584 3*366755

'ý8138'15162 1.43809:6 9.54 49.54' 0.15 16.41

'110 0.7w.

0.810560 3.3324433 8.6800973 21.60273 52.08 52.07 0.29 17:57 1 09 U075 0.758528 3332626 8.722933 1 22.03502

,54:61.

54.60 0.43 18.74, 1"08 0.7826087

.0.700175 3.280803 8.42537576 1.74844,

.5,1

.57:.1

.0.57 19.91 107 0.8181818 0.633515 3.t3534 79;8406023 20.59328

'59.67 0.77 0.71 21.08 1,06 0.8571429 0.555249

-2.926f 51

.6.7'248'554.

18.40422

.62.21 6220 :

085 22.25 105 0.9 0.459044 2.553258

..1201059 r 14299762 64.74' 64.73, 01199 23.42 04 0.9*473684 0.328838 1.925107

,2.9107112 10.1683 67.27 67.26 1., I3 24.591, 103 1

0.000000 0.000000 0

3.685426 Total VOlume=

I,*36:4.'97 cufeet*

amn-b ie nt t e m p",=

85.00 degE.

temperature~of:caIcuIation =

103.00

-degF 12/32 8:6PMCaI8,(10

m m

nm m

m m

-n m

m mm MULTIPORT SUBAQUEOUSDIFFUSER IN AN

'ARBITkARLY DENSITY sTRTFIED ENVIRONMENT AA-15.00 FEET i-,----

A= 7.50 FEET JET DISCHARGE ANGLE=

.6.00DEGREE'S W/HORIZ JET DISCHARGE "ELOCITY 13.02.FT/SECz S:JET DISCHARGE TEMPERATURE= 115.00 F JET DISCHARGE DENSITY=. 1.016851 GRAMCC.

JET DISCHARGE DEPTH-34.00 FEET To.a. JET JET-TEM End Area Volumerc

??...

,:.. ?£....

W IDTH I),.,cd~eviations widtfil........

0 0

0 7.5 115 7.5 44.178609 46.84

. 46.84 0.00016 15.15771 11 1.0679 G;6521i431 0.924653 3.503904ý

'96425972 1260.493 47.01, 47.01f, 0.01 5.2,4 111 0.6538462 0.921828 3.511477 '9.684322:5

.1.660845 49.54 49.54

0. 15 16.41.

110 0..68 0.878251 3.602059.

10.1904 25.16458

... 5222028

5:2.07: :o i14 17227

". i 0

2 :...

7.29 17.57 0

0.7083333 0.830470 3.648709 10.456058' 26.1417

.54.61

'54.60 0.43 18.74 **

.8 j07j91304 0.777536 3.643291 10.42503.1

ý26.4388

.57.14 57.14'.

0;57 19.91 1-07

'0j727273 0.718093 "3.574551 10.0035355 256"9612 59.67

'59.67.

0-.71 2

106

8095238 0.650091 't. (3425966, 9218403'.

2.37833,

.62.21 62.20 0.85 22.25 105 0.85 5.570121 33.171084 7.89777,96'21.67183l 64.74' 64.73 0.99 23.42 104

'08947368 0.471647

2.761151 5.9878368.

17,582i!

67.27 67.26 1.13 24.59 103 "0'.9444444 0.338108' 2.0781150 13,391:9035 11.87625 69.80 69.79 1.227 25.75 1:02 1

00000 0.000000 0

4.294693 Total Vo'ltume6=

1,445,i6f cu~feet

'amnbient tempi."

85.00 degF.

temPefature of caleaulation =

102.00

.deg F.

12/j'/2 8:46 PM 12C/84 186C 1

Y.i 102.

m7 m m

m

-m

-m m

m mm m

m m

MULTIPORT-SUBAQUEOUS DIFFUSERIN ANAXRBITR'ILY DENSITY STRATIFIED pENVIRONMENT AA= 1H1 5.00:FEET'

'1---&,AA-.---- I A= 7.150FEET JET DISCHARGE ANGLE

.0,0 DEGREES ZORZ JET DISCHARGE VELOCITY= 13.02 FT/SECQ

,*JET DISCHARGE TEMPERATURE 115.00 iF, J1ET DISCHARGE DENSITY= 1..016851 GRAM/CC' JET DISCHARGE DEPTH= 34.00: FEET

!*S* )*

yTotal JET:

Ai::.

.T:

,T ti~dii'i0-de~gjetll:

/.T JET..... TEM101 dege End Are4a, Volume WITotlJTH E

E CL) deiatio ns width 0

0 0

7.5

[1.

5 7.5 44.178609 46.8 46.84:

0.00016 15.15771 111.0679 0.6137817 0.988044, 3.744 123 11.01006 1292519 S47.011 47.01 0,!0l 15.24 L1 1

0.6153846 0.85401 3.753645.

11.066134 1.897102 49.54 49.54 0.15 16.41 110 0.64 0.944761 3..874845 11.79229, 28.94243 52.08 52.07 0:

.29 17.57 109.

- 0.6666667 0.9900517 3.956461 12.294284310:.49746 54.61 5.. 60 0.43 18.74

.8 0.'6956522"0.851945 13991,952 12.515847

'31.44i36 57.14 57.14 0.57 197.91

107 0.7272727

ý0798065 3:,3972635.12:395011i 3:.54 1 13 59.67

'59.67 0.71 21.08 106 0.7619048 0.737474--

3.886472 1.1863!1i65:.. 30.0,7 1473.

62'.21 62.20 0;.85 22125 1f05 0.8 0.668047

',3.715762 10.843897 287-5078 64.74 64.7:3 0"9.9 23.42 104 0.8421053 0.586260 3.432123

.92515659 25.44*07 67.27 67.26 1.1 24.59

'103

.0.8888889, 0.485351.

2.983]1721 16.9894993 p,20.56379

.69.80 "69.79 "

.27 27 02 0.94117651 0.348209*

2.241962' 3.947.7.1.78.13.842

.72.34 72.32 1.41 26.92 10l1 1

0.000000 0.000000 0

4.998443 TotaiVolume =

1,;541.13 cu feet ambient temp =

85.00 cdegF.

tempe~rat~urei'of'calc~ulation-.

1091.00QI dlegF!

12/3/21-8:471PM C,.8.

10 Calcl&x

mm mm m

m--*

m m

-m m m

m m

m st...ar.

101:Ig End Area, Volume' I.(AT CL,, deviations:.jbf*wi~dthx....

S X

JET WIDTH JET TEM AMBTEM DELTA T w

0 0'

1,4792 113 85 28 1.......

'1A792o 171848 9.33539 9.33539

.0.0005

.3.63464.,

4108-7912,

8

,391 0625 0896.

0678 0.56 9692 9.74421 9:744195 0,'.00553 3.2242,2.08ý 823 0.69565 0.J85s195,,

'.6 867t6 0.3037

.. 4903 u1.ýjb2692 I10.2'608 t.-01,245 3'3.46382

107'

,85

'2 0.22-.9 06 06910 0b§51 0.126

.10,.77762 717.

7757.

.0,*0938 73.70343 106

. 85.

2,70;6'190.

0.73747 0.68280 0.3661*&

0A91951 1"1.29433 11.29426 0.102630

3.94304 105.......

.85 20 080000 0.66805: 0.65853 0:34060 4

0.18259 11-8-1104 11-81095 0.03323 4.18264

'104

___o

_ 85 19 0.84211 0.58626ý 0.61303 0.29516 0..

.16425

'12.32774 12.32764

,0.04015 4.42225 103 85

18 0.88889 b.485351.

0.5153659 0.22614-0.13468 12.84445 12.8443' A004708 4.66186 102

85 17 0.94118, 0.34821.

0:0582 0:12935 0.09184 13.36116 13.361Q02

'0.05401 4.90146 101 85

1. 0000 0.00000

,0,0,00 0.00000'.

0.03342

13,8778"7

'1.3.87771 A006093

'5.14107 100 85 15 1.06667.

1:439457 14.39440 0.,'06786

.38068 99 85 14 I..

1*'83' 1

6;23_7*

14;118 14.91109

'0:07478 5:62028

-:9,8

'51

.37'_________

15.:08733 15.08713 0:*

0-7714.

5.70192 97.65929 S 8. 5 1l 12.65929 '1.26389

__ 1..

.i.

15.88106 15.88063 0.10850 6.06954 97

.85 12 1.33333

'17.08498 17.08421 0.15608 6.62714 96 85:

11 1.45455....

18.014421 18.04317 0,.1.9398 7.07142

,95.2032'........85 10120324 1.5'6813

,18.A0951 18.40816 0.,'.21736 7.24025 1..

951 3085 10 600)00,.

.201.20687 2

20.20402, !033241

.07097

'94

8.59 1.77 78'....

o,,l.9

_.7_7 77.8.

21.16309 21.159431 :Q039361

,851292 93.46799V 85 8.467599 Total Volume =

10.8 cu ft:

am temp=

85;00 deg F.

"ft'emperature of calculation =,

101.00 dek.F.

12/3/2009 10:25 PNM1

Cal*SB*Is*/*01*

m m

Mu L""TI PO

'SUBAQUEOUS.DFUE A

ABTR.ARL DENSIT STRATFE EVRNMNT AA= 115.00 FEET A= 7.50 FEET I-"ýAA -

1--

JET DISCHARGE ANGLE=ý

.00 DEGREES WiHRORZ.

A

- - - - JETDISCHARGETEMPERATURE 115.00 F JET DISCHARGE DENSITY= 1.0-1685*1: GRAM/CC JET.DISCHARGE. DEPTH= 34.00 FEET Total JET J.E-TT/

(AT sta*d6ad' 100de'gjetd

'"e Volume

'::S~

.: *X,'

T talJE T E4

.:-.:-,F.

lm

~ d'Area.

Vbl*,

umeý WIDTH 4.*_E____

CL)-

deviations widtlh t

0 0

0 7.5 11i5:

h5

>44. !7896090 46.84 46.84 0.00091!6 15.15771 110679 0.5754203 1.051337 3.983964 12.465807 1326.612 47.01 47.01 0.0'0.1 15.24 1l1 0.5769231 1.048853 3.995349 12.537154 2.148612 49.54 49.54 0.15 16.41 11.0 0.6 j 1.010768 4.145563.

13.497599 32.96417 52.08 52.07 0.29.

17.57 1609 0.625.

0.969540 4.259717 14:*251184 35.1344 54..61 54.60 0.4*3 18.74 t

108 0.6521739 0,,924602 4.332397

.14.741644 36:.70956 57.14 57.14 0.'5,7 199;4.9 107' 0.6818182 0.875205 4:356628 14.907011 37.53994 59.67 59.67 p0.71 21.08 106 0.7142857 0.820332 4.3231313 14.678671i 37.46021 62.21

,62.20 0.85 22.25 105 0.75 0:0.758528 4'.219026 13.980215 36.28674 64.74 64.73 0.99 23.42 104 0.7894737 0.687588 4.25327 12.726, 33.81434 67.27.

67.26 1.13 24.59.

1.03

.0.8333333 -0.603857 3.711I555 10%819.35,4

.29.81219 69.80 69:79.

1.27 25.75.,

02

'0.8823529

.0.500326 31323.221380:,. 8.15029851,.

24.0 1862 724..2.3

1.

26.92 1...

01 "0.975

'0359273 2..48t60 4.5926T*12

.1 3456 74.87 "

4..*,85 1,565 28.09 100 1

0..000000.0,0000

0.

5.814981 Total.Volume=

1:,654.,45,

'c feet

,a

,mbient tem "-,

85.00 degP.

'eperature ~of calculation

'10o.00 dW gF.W 12/3/2009 8o9:47", PMC

_a c, x

m m

m m

MULTIP'ORT SUBAQUEOUS DIFF.USER INANABITRARILY'., DENSIT Y SRTFE NIO N

AA= 115.

1

.- FEET

A 7.50 FEET I

JET DISCHARGE ANGLE-=.

.00DEGREES W/HORIZ

JET D)ISCHARGE VELO,'C-IT,,Y=" 13.02 FT/SEC`

j**********

JETtDiSCHARGE TEMPERATURE-115.00 F JET DISCHA:RGE DENSITY 1.0 16851 GRAM/CC JET DISCHARGE DEPTH=.,34.06 FEET Totl JET6Tsa r

WIDTHp JET TM F

T,

-*i"*di' 4d 99 deg jet End.Area,,i ue WIDTH___________

CIL)-

deviapiips, width 0

T0 0

7.5

'S

"._ 7.5 44"1"

-678609,

'46.84 46.84 0.00016 15.1.5771, 111.0679' 0.53,70,59

1.

!-115031 4.2-25330 i40220217..1363.059 47.01 47.01 0.01 15.24-11i 0.5384615 6.:12690

.238519 14.109702 2.41748 49:54 49.54 0.15 164,1 Ito0 0.56 1.07686 4.416652:

15.320605 37.26348 52.08 52.07

.0.29 17.57 109 0.5833333 1.038264, 4.561662 16,343147 40,09138

.54......

.6 54.60 0.43 18.74 108 0.6086957 0.996431 4.668965 17.121063.

42.37105 57.14 '57.14 Q0.57

19.91 1:07, 0.6363636 0.950773 4.732 794.592385 143,95278

,....."59.67 59.67

--0.71 21108 106 0.6666667 0

0.900517 4.745705 17.68"8499 44.67125 62.21 62.20 0.85 22..5 105 0.7 0,844600 4.697773 17.332'997 44.34282 64.74 64.73 0.99 23.42

104z, 0.7368421 0.781513 4.575191 16:.440234 42.76232 67.27 67.26,,

1.13 24.59 103) 0.7777778 0.708963 4.357582 14.91354 39.6989

.69.80

'69.79 1."27

.25.75

'102 0.8235294 0.6233147 4.012169 12.642935 *34.89091 72.34 72.32 1.41 26.92 101 0.875" 0.51678.1 3.478302 9.50210974 28.03928 74.87 74:85 1.55 28.09 100 0.9313333 0."371464,,.

2.6087381. 5.3450351 18.79897 L-78.32 783]0 1.911 29:671 99 1

0.000000 1, '0600,.1

0.

9.2363 Total Volume 1,79.60 cu.feet amtbienit temp -T 85.00 deg...

pte

-t e f alculati on 99.00 degi'F 12/3/2009 8:47 PMCll.lxI9

.'Calc18AIýxYl 99

I m

m

m.

MULTIPORT*

ISUBAQUEOUS DIFFUSERI'N AN ARBITRAMLY DENSITY STATIFIED ENVIRONMENT AA= 115.00 FEET' A= 7.50 FEET i

~

JET D!ISCHARGE ANG LEO=:.00DEGREESW/ORI

JET DISCHARGE VELOCITY-13.02 FT/SEC

.JfTVDSCHARGE TEMPERATURE 50 JET DISCHARkGE DENSITY-1.016851 GRAM/CC JET DISCHARGE DEPTH4=, 34.00 FEET Total JJET ETTM AT/

(AT standard 98-de-gietE-dA/

Vlm s*

1.

7 !

JEl-~,

i:_.

End Area>tý M:V uiume.

___._.____..W IDTH:

-CL)

'deviations:

width N___..

0...

0.

0 7.5 115 7.5 44.178609 46.84 46.84 0.000016

15. 1'5771 11.1f0679. 204986976 1.179623 4470096 15.693 1402.20,8 47.01 47.01 0.01 11.177410 4.485055 15,798838 2.70622*

49.54 49.54.

0.15

.16.41 11M 0.52 1.143614 4.690419 17.278767 41.88154 52.08 52.07 0:29 17.57 109.

0 0.5416667 1.107343 4..865163 18.59'020,7£. 45.41586

.54.61. =

54.60 0,43 18.74.. 108 0.5652174 1:.068218:

5.005339 19:676891 48.45227.

57.14 57A4 0.57 191 107 0.5909091

.1.025761 5.106071 20.476851 50.84107, 59.67 59.67 0.1 21.08 106 0.6190476 0.979360

..5.1.61208 20.921475 52.41691 62.21 62.20

0.85:

22.25.

105 0.65 0.928206 S.*1,62797 20.934352 52.996:18 64.74 64.73 6099 23.42

104,

0.6842105 0.871194:

5.1::0100206 20.42984 52.37369ý 67.27 67.26, 1.13 24.59 ii:.

1 030.722222'2 0.806750,.

4,.9958618 19.311267 50.3186 69.80 69.79 1.27 25.75 102 0.7647059 0.732481 4.716121 17.468653 46.56927 72.34 72:32 1.41 26.92 101 0.8125 0.644421 4.337409 14.775778 0.082661i 74.87 74.85 1.55 28k09 100 0.8666667 0.534978 3.757072 11.086349 32.74559 78.32 78.30 1.91 29.67 99 110.9285714 0.'384988 2:855774:

6.405266 30.22577 8k4.27

_84.211 2.89

,32.3 98 1

0.000o000,0.00000 0

19.0344 Total Volume =

1,96901 ~U feet amnbient itmp 85.0Q deg F.

temperature of calculation =

98.00 degF.

.2/3/2009 8:48, PM9 CalO.&x1sxY1ý98

-l*m m

m m

- m

'MULTIPORTS*UBAQUEOUS DIFFUSERN R. AN:i4ARBITRA.RILY ENSITY STRATIFIEDENVIRONMENT

AA= 15.00` FEET:

A= 7.650 FEET JETIDISCHARGE ANGL,(EF

.oo PE1GREES W/HORIlZ J JET. DISC HARGE YELIOCTY 13.O2Th'I PECý SHb........DSCHARGE. TMPERATURE

.00'F JET DISCHARGE DENSITY= 1.0 16851 GRAM/CC JET DISCHARGE DEPTH-34.00 FEET S

~~~~~Total JET JET

'-M AT/

(T

standard, 97 deg jet(A dAra Vlm Y_ _

WIDTH

,CL d'eviations' vicdth 0

0 0

7.5 115 7.5 44.178609 46.84 46.84 0.00016 15.1577,i 111.0679:

.460,336.

1.245631 4.720228

!17.499087 1444.492 47.,01 471.01 0:0.1 15.24.

01.461538'_

1.2:435.35 :7643 176 324 3 8.2I

~

41.7

rSi i

369*43-17.*623244,:

..01:!*2 49.54 49.54.

0.,15ý 16".1-o 10.49 1.21 t 585 4'.96919,5 19:393744.'466:8694:1 52.08

.52.07 0.29 17.57:'" 109 0.5' 1,177410 5.173004 21.017217 51'. 16675 54:61 :

54.60 0.43 18.74 108.

0.521739 1.140691 5'344923 22.4A37..96

-55.0205 57:.14 57.14 o.53, 19.,.I 107

'0.545455 '1.101032 5.480756., 23,.5923 12 58.2809,8 59.671

.:67 0.71, 21.08

106,

..."0.571429 1.057937 5.5375309 A*4.13355 60Q78286 62.21 "62.20 0.85 22.25 105

.6' 1.010768 5'622016 24.824113 6 f2.*34252 64.74 64.73, 0.99 23.42.

104

.0.631579 0.958679 5...*1364' 24.738943 62.75476 67.27 67.26 1.13 2419 103 1 0.666667... 0.900517.

5.534949 24.061174 61.78876

, 69.80 69.79 1.27 25.75 102

-0.705882

.0.834634* :*5.373839' 22.680826 59.18286 72.34.72.32 L411.

26.92 101

.0.75 0.758528 5.105426.20.471679' 54.63798 74.87 74.85.

1.55 28.09 100 0.8 0.668047 4.691596 17.28744 47.80909 78.32 78.30 1.91 29.67 99 0.857143' 0.555249 4.118737 13.32348 52.89612

.::847 8.21 2.89 32ý.`361 98 0.923077:

0.400107 3.236735 8.2281793 64.04463

.. 90.:21i J '903 3.9,6 35.0'5 97 1

.000000 0.000000 0

24A451,51 STotal Volume =

2,209.54 cu feet Amfbienit temol:p; 85.00 deg'lF.

temperature of~calculation'.

97.00.

deg F.

1"2/3/2069 18:48 PM C~l.lx19

i:m m

-l l

m m*

MULT*PORT SU:BAQUEOUS DIFFUSER IN AN, ARBITRARiLY* DENSITYSTRATIFIED ENVIRONMENT AA= 11 I5.00 FEET I'----AA---- 1

.A= 7.-50 FEET

-A--

JET DISCHARGE ANGLE:

00 DEGREES WIHORIZ JETDIiSCHARGE VELOCITY= 1302-FT/SEC

-TDSR JETDISCHARGEDTEMPERATU E=1015.00E JET DISCHARGE DENSITY= 1.0 16851 iGRAM/CC JET DISCHARGE DEPTH= 34.00 FEET Total JET JET TEM[

AT!

,(A standard

.96 deg jet S YEnd Area Volume

,WIDTH CL)

deviations width 0

0 0

7.5

[15

'7.5 44.1786090, 46.84.

46.84, "0.0006 15.15771 11'1.0679 0.421i9749 377898 i9.,6i736' I4900.457 47.01, 4'7.01 0,01 15.214 I: i 0.4230769 1.31164.1 4.996376, i9.606486 3,3573

.49.54 49.54 0.15 16.41 11 0.44 1-281390 5.255495 21.692855. 52.29158 52.08 52.07 0.29 17.57 109-0.4583333i.1.249127 5.488094 23.655527 :57.41831.

54.61 54.60, 0.43,

!18.174.

108.

0.4782609

.i,214577'

!5.691133 '.25.4382351 '62.16056 57.14

57. 14 0.57 19.91 1,07 0.5 1.177410 5M860953 261979011 66.36863

.. 59.67 59.67 0.71 21.08, 106-

ý0.5238095 1.137213 5.993092 '28.209244 69.9877137 62.21

',62.20 0.85 22.25.

05 0.55

1.093469 6.082*l1) L'29.052523 72.50256 64.74 64.73 r

0.99

-23.4'2 104

.0.5789474' 1.045508 6.120688.

29.423204*. "74i03963 67.27 67.26 1.13 24.59 103

.06111111'H 0.992448 6.099997 29.22461.7' 7.25753 69.80 69.79 '

21.27 25.75 102 0.6470588 0.933079 6.007685 28-346781 72.89461 7'..... 72 72.32 :;'

1.41 6926.92 101 :

0.6875 0.86567.1 5.826579 26.663476 69.65179 74.87

74.85 1.55 28.09' 100 507333333 0-78758 5.531180 24.02841 64.18404 78.32 78.30 1.9]

29.67 99 0.,7857143 0.694496 5.151644 20.844007 1 77.5402 4

84.27

8.21 2.89 32.36.

98 0.8461538 0.578021 4.676003:* '17.172719; 12.9735

..0.2 90.13 3286 35.05

'97

" 0.9,166667 0471663.::-1654965

10.49ý1,943 82.21051 98.24 98.06 5.81 388.59.

96, 1

, o:ooooo i0000000 0

42.13031 Total,. yolume=

2,544.32. tcu feet ardbje t temb 18.5.00

degF, temperaturie of ca1~lwiationý-

96.00 deg F.

,l2/3/2009 8:4.8 PM ac8xsYI9 06-1c I &xIs'.x 'Y1 -96

MULTIPORT SUBAQUEOUS DIFFUSER`'IN AN A9BITRARILY DENSITY SRATFIEDENVIRONMENT AA, 42'.00 FEET lr----AA-1--

A=- l.48 FEET:

.Aý JET DISCHARGE ANGLE

.00 DEGREES W/HORIZ:

JET DISCHARGE VELOCITY= 11. 54 Fr/SEC AT JDISCH"i~GE:TEMlPERATURE=I113.010-F JElT.DI.SCHARGE DENSITY= 1.017362 GR:AM/CC JET:DISCHARGE DEPTH= 26.50 FEE T X,

Y.

JET WITH DILUTION JET TEM JET DENS AMB DEN AMB TEM DELTA T; ALLOW T 9.33539

'15.08713 24.1049 0,3.9.75 29.79727 35566215 38.4002 41.189.72 431.92667 46.6034 49.2131, 51.75012 54.21018 58.88924 61.10639 63,24258, 65.29939

'67.27898 69.18401

,C).0005 0.07 7 14

`0.19398,

,0.393611 1;48931 2.07932; 2".7ý9513P 3.64318 4..62753 5.74976 7.00888 9.92278

'11.56155 13-32197 15,1837 17.14204 19.18842 21.31461 23.51289' 2S.77611 43.3464

,5.70192 7.07,14 2

'8.51292 9g.87186

'11.22065

'12.48117 1 5.0873

'16.34723 17.571!29

'183'5531

19. 8964 3

20.99'3*34 2,2.04634

23.05716 24.9645 25.86874 26.74555

.27.59901 28.4329 29.25064

1.

025 77 1,927-78

2.88194

3 3.468 4;25341

ý4.72195

5.192,79 5.6666 6.144.5.

6.62624

7. 11369 8.10798 8.61638 9.6591 10.19458 10.7401

11. 29605 11.86273 12.4404 108.7912 97.6592 95.20324.

93.46799, 92.2918,3; 91.40116,

'90.73758 90.16827 89.69965, 89.30669

,88.68298 88.43061 88.2'0799 8 8. 0099 1

.87.83231 897:67204 87.52656 87.39384 87.27225 87.61604Z9 87.05722 86.96169ý 1.01828 i1.02:12:2; 1.0216 1.102, 186 1.02205 1.02219.

1,02232 1,02242 1.0225 1.02258

1.i02264*

1.02269

'L.02274:

1.02278 1.02282 1.02286 1.02289 1.02292.

1.02294 1.02297 1.022ý99 1.02301 1.02344 1.02344 1.02344 1.02344

.1.02344 1.02344 1.02344 1,02344 1.02344 1*02344ý 1.023144 1.02344 1.02344 1.'02344 1'.02 344 1.02344 1.02344 1.02344 1.02344 1.02344 1.02344 85 885 "85:

85:

85 85 85.

85 85

85

,85

'85, 85 85*

23.79118 12.6592q

'10.20324 8.4679 9 7.29183 6.40116 5.16826,-

4i69965 4.30669 3.97195 3.68298 3.43061 3.20799 3.0099 1 2.83231 2.67204' 2.52656 2.39385 2,27226, 2.1604S, 2,05722!

1.9617 17 17 17 17 17l 17 17 17 17 17 17 17 17 17 17 17 1717 1717 17~

THIS IS, FREE SURFACE 112/A/29Qp B:SS PM 12/3/2009 8:55 PM CaIcl8B.xlsx PSL-5{SAA)

MULTIPORT:SUBAQUEOUS DIFFUSERIN AN ARBITRARILY DENSITY:STRATIFIEDAENVIRONMENT A= :42.00 FEET 1,

A,= 1.48 FEET

.JE.DISCHARGEANGL=

00. DEGREESKWHORIZ JET DISCHARGE VELOCITY=, 1154IFT/SEC:

~~ JET DISCHARGE TEMPERATURE, 113.00 F JETDISCHARGE DENSITY= 1.017362 GRAM/CC JET.DISCHARGE DEPTH;,R,26.5

.FEET S

"C

,y JET WIDTH JETTEM'.

AMBTEM DELTA T A933539%

9.33539 0.00005.

9.74421, 9§.74419, 0:'00553

,10.260921 10.26088 0.01245.

10.77762.'

10.77757 0.019,3&

11.29433-11.29426 0.'0 263 0 11.81104.

11.81095 0.03323, 1,232774:'

12.32764

0.0.4015 12.84445 12.84433, 0.04708 1

'13.87787 13-.87771 0.06093 14.39457 14.39440 0.06786 14.91128 14.91,109 0.07478 15.08733 45.08713' ý9.077-14'

.15:.88106, s15.88063*

0.108-50

,17.089498 17.08421

-0.451608 "18.04421 48`:04317: '0.19398, 18.40951k 18.408'16 0.21736 20.20687 20.20402 0.33241 21.16,309, 21L15943 0.39361 241!417 24.10491 0.:66866

,27.059741

.27.03975 1."039,95 29A83447 29279727 1.4893 1 32.76206 32.69601 2.'07932 35.67591 35.56625 2.79513' 38.57263 38.4002 3.64318' 41.44885 41.189712 4.62753 44.30138 43.926667 5.7497.6 47.1275 46.6034A 7.00888 49.92511 49.2131 8.40164 52.69285 51.75012 9.92278 55.43019 5421 11.5655 58.13732 56.5904 13.32197

.60,81519 58.88924 15.1837 634

.27 61.10639 17.14204 66.08948 363.24258 19.18842 63269005 6.65129939, 21.31461 71.26933 167.278 19 18 23 1 5289 73.82977, 69.18401 25.77611 THIS IS FREE SURFACE 3.03464 3.224:22 3.46382.

3.70343 3.9430,4 4.18264 4..42225 4'66186 4.9.0146 5.14107 5.38068 5.62028, 5:7,0190 I6:06954

.6:'ý627 14.

7.07142 7.2402,5 8.07097 8.5129ý2 9.8718,6 1-1.220665 12.481,17 13.79679 15.08735 16.34723 17;57129 18.75531 19.89643 20.99334 22.04634 23A05716 24.02867 24.96415 25.86874 26.745,55 27.59901.

~28.4329.

29.2 50'6'4 108'.7912':: !

1058 107.

1063

'105 103';

.1023 99 98 96 95120324 95 94 93.46799.

92.29183*

91.401'16:7 90.73758 90.16827 89.69965 8930669 88197ý195 88.68298 88,43.061.

88,20799 88.00991 87.8323i 87.67204 87.52656 87.39384 87.27225 87:16042':

987.057.22' "69669 85 23179118"

,85, 231]

85,

22.

85

.21' 85 20 85-'

19 85' 18

'85 1'7 85<.16 85' 15-

.85 14'

85 13 85 12.ý65929 85ý

.12:

85',1 85" 10 85 n

S85

.8.467:9 851 7.29183'

85i 6.401:

85' 5.73758 85 5.16826 85 4.69965 85ý 4.306695 85, 3.97195 85 3.68298 85 3.43,061 85 3.2607 85'.

3.00991 85

-2.3231 85 2.67204 85 2.52656 85 5 2.39385 85'

,2.27,226 85' 32.1604395 85 32.057298' 85 3*41611

"' '- ýV-2/31200'9 8:S

ý ""_:'

12/3/2009~

~

8:tM aclBxlx L-S(SAA) (2),

Temperature -

O.F.

1I09:

108 107.

106 1.04%

'103 102 101 99 98 95.7 96 94 Proposed (115 deg F dischar'ge;)

'501.25

518;75:

539.48 5938.46 628.46

,6'70.27 78.0.43 855.12 957,13 1,098.4 Existing (113:

d eg F 473.88

..486.415 50'1.25 518.7S 539.48 s93A.:6 62~l 1

8.46 670.,27 720.34 957.13 1098.4:5 130436ý 12/3/ bO§ý9:53 P...

M" 12//209 8~53PMCaicl8B.Xlsx Ta'ble "r

n m

m m_ m m

m

-n m

m H

m

mml, mm m

TI/

sýtandard 108de8g S

x, Y

JETWIDTH JETEL AMBTEM6f DELTAT"

('ATCL) deviations... jet width' iEndArea Volume 0'

O 1.4792 113 85 28 l

1.47920 1.71848 9.33539 9.33539 0.00005 3.03464

108.7912 85 23.79118 0.,96674 0,26008 0.19731 0.03058 8.16405 9.74421 9.74419 0.00553 3.22422 108

.8 185 23 1.00000 0.0.00000.00000 0.00000 0.00625 10.26092

10. 26K8 8

-0.01245 3.46382 107 85 22 104545

-1077,762 10.77757 0.01938 3170343 106 85,,

21 i;09524,

11.2943'3 I1.29426 12 0.02630 3.94304 105 85 20 1.15000, 11.81104 11.81095 0.03323 4.18264 104 85 19 1.21053.

12.32774 12.32764 0.604015 4.42225..........

i03 85

18 1:27778 12.84445 12.84433 0.04708 4.66186 102 85, 17 I35294. :__

13.36116 13.36102 0.05401 4ý90146 10 1 85 161.43750 13.87787 13.87771 0.06093 5;14107 100 85

15:1.53333 14.39457 14.39440 0.06786 5.38068 99

85.

14 1.64286, 14.91128 14.91109 0.07478 56,2028 98 85

13 *1.76923 15.08733 15.08713,

'007714 5.70192 97.65929 85 2.. 65929 1.81685 15.88106 15.88063 0.10850 6.06954 97 85 12 ý1491667 17.08498 17.08421 0.'15608 6.62714 96 85 411 209091 18.042421 18.04317 0.19398 7.07142 95.20324 85

.10.20324 2.25419 18:.40951*

18.40816 0.21736 7.24025 95 "85 10

!,2o3000__

20-20687 20.20402

-033241 8.07097 94 x85 9 2.55556 21.16309

'21.159431' 0.39361 8.512921

'93,467991 85 8.46799 T6tal Volume:=

8.2 cu ýft a M. bienttemnp,=

85.00 deg F,.

temperaturemof calculation =

108.00 AdegF.

1/5/2010 11:36 Pm at8xs'10

'CýIelBRý 1§ 108

mm-m n m mm m

m

~T tnad 17dg End Area

X Y

JETWIDTH JET;TEM.

AMBTEM DELTAT

(*TiL) deviati6ns Jetwidth' ue 0.0 0

1.4792

1. 13....

85 J2'8 1.47920 1.71848.......

9.33539 9.33539 0.00005 3.03464 108.7912 85 23.791180.92471 0.39566 0.300

.07077 8.35164 9.721 9.7449,0.00553 3122422 08 85 23 0.95652" 0.29817 0.24034 0.'04537'..

0.02374 10.692 106088 0.01245 3.46382

10.

85 221.00000 0.00000 0.00000 0.00000 0.0172 10077762 1017757 0.'01938 330343 106 "285

.12 104762:"

000000 11.29433 11.29426 0.02630 3_94304 105 85 20 1.1*0000,___

1181104 11.81095 0.03323 4.18264 104 85 19 1.15789I.

12:32774 12,32764 0.;04015 4M42225 103 85 18,122222.

12.84445 12.84433 0.'04708 4 66186 102 85 17 1.29412.

1 3 : 3 6 1 1 6 1 3.3 6 1 0 2 0 0 5 4 0 1 4 9 0 1 4 6 0 1 8 5 1 6 1 3 7 5 0 0 '

13.:87787 13.87771 0.06093 5.1.4107 100 85 1 51.466671 14.39457 14.39440 0.06786' 5.38068 99

.85 14 I.57i43 "

14.91128 14.91109 0.07478 5.62028 48 85 1

1O.69231...

15*08733 15.08713 0.07714 5370192

-97.65929

85:

2.65929 1.73785 15.88106 15.88063 0.1 10850 6.06954 97 85

.12 '1.83333 '.......

i7.08498 1708421 0.15608 6:.62714 96 85, 11

00000,

18.04421" 18.04317 0:19398 7-07142 9520324 85

100-20324

-2.15618 8.)951 18.4.0816

0.21736 7:.24025 95 85 10 2.2:20000 20.20687.

20.20402 0.33241 8.07097 94 85 9 2M44444 "

21*.16309

21-159431 03936'1 8.51292 93A46799 85 8&.46799 Total Volume ý::"

8.4.cuft.'

ambient temp =

85.00 deg..F.--

-temoperature of calculation=

107,00' deg:F.

1/5/2010 11:36 PM CllBxs 0

CalC18B3.'IX:k107'

m ml m

-l m

m

,,&T/

sta6ndard 106 deg 6ý th.

,,E~nldlArea, Volulme

aev!.~~~~~~~ya~tion~s*

jet iw d~h

..S.

X; Y

JET WIDTH JET TEM AMB TEM DELTA T

.L ia.on

.0 0

0.

1.4792:

113 8

281 ' ]'

,,_,i47,920 1, 71848.

9.33539..

9.33539

ý0.00005 3.03464 108.7912 85

2379118 0.!88268'

`0.4.9959:

037902 0.11282

8.54795 9.72

.....74419 0100553 3.22422 108 85 23 0.91304 0.42655 0:34382 0.09284 0.04204 10.26092

'1026088 0.'01245

346382 107

.85 22 0.95455 0.30502 0:26414 0.05480 0.03814 10.77762 10.17757 0.01938 3.70343 106 85 21 1

W00000 0.00000 0.00000 0.00000 0.01416 29433.

41.226 0..0,2630

3..94304 105 85 20 1.05000 11.81104 11.81095 0.03323 4.18264

, 104 85 19 1.1052617 12.32774 121.3276'4 G004015 4:42225 103 85 18 1.16667 12.84445 12..84433 0,.04708 4.66186 102 85 17 1.23529:...........

[:13.36116 13,36 1 021 0.05401 4:90146 101,8 16 1.312_.250 13.87787

.13,87771 0.06093 5.14107' 100 85 15 1.141000 1_______

14.39457 14.39440 0.06786 5.38068

'99 85 14

.1.50000:

14.91128 14.91109 0.07478 5.62028.

98 85 13 -1.61538' 15.08733 15.08713 0.07714 570192 97.65929 85

-12.65929' 1.6'5886

.1.....

i15.88106 15.88063 0.10850 6.06954.

97 85 12 1.75000"-

17.08498 17.08421 0.15608 6.62714..

96.

85 ii 1.90909 18.04421 18.04317 0.19398 7.07142:

95.20324, 85

".10.:20324 2.'05817:..........

18.40951 18.40816 0.321736 7T240251 9

85, 10 2

.10000.....

20.206871 20242 032187974 85 2 =3333 21.163091 21.159431 0.39361 8;51292 93.46799 85 8.46799 Total VolumIe1=

'8.6 cu ft,

ambient temp =

85.00 deg F:

.'temperatureof calculation =

U06.00' deg!F.

1/5/2010 11:36PM Calcl8B.xlsx 106 6al.t8B.xlsx; 106'.

Ill B

m m

m

-l m

m AT/

standard 10.5de EnAra Vlm S

____X JET WIDlbTH JET TE4 M

AMBTEM, DELTA T (TC) dvato e

it 0b0 0

1.479,2 11 528:

,1.47920, 1.14 9.33539 9..33539 0.00005 3.03464.

108.791;2 85 23.79118 0'.84065 6.5892194

ý0.44701

.0.5694 8.75385 9.74421 9.74419 0.00553 3'22422 108.

85 23 0.'86957

.,0.52870 10.42616:

0.14264 0.06124 10.26092 10.26088 0.01245

346382 107 85 22 0.909096 0.43 0

660:

0.37808 0.11227 0106586 10.77762 10.777 0.01938 3.065 21:

,0.9523 0.31238 0.28922 0.06570

.0.04598 11.29433

'1-294.26

-0.02630 3:94304

'105 85 20 1.00000-

.o000.000

0. 00000 0.6006000 0.01697

i.11.81104 11.8,1095 0.03323 4.18264 104 85 19 1.05263T

'12:32774 12.32764 0.04015 4.42225 03 85 18 1111,1t...

12.84445 12.84433 0.04708 4'66186 102 K85

" 17 7647 13:36116 13.36102 0.05401 4.90146 1:01' 85 16 :.1.25000, 13.87787 13.87771

,0.06093 5.14107 100 85 '

15.

1* 3333 :3:",

14`39457 1.i39440

0. 06786 5.38068 99 85 14, 1.42857:`

14.91128 14.91109 0.07478, 5.62028 98

_ 85 13 1.53846......

15.08733 15.08713 0.0714 5.70.192 97.65929:..

___8 2.52 1.57987 7715.88106 15.88063 0.10850 6.06954 97' 85 12 "1.66667 17.08498 17.08421 0.15608 6.62714 96 85 11 1.818189_

___s_

8.04421 1804317 32485 "02032 1.96016

18240951 18.240816 0.217361 7.24025, 95 85.10 2.0.0000 20.20687]

20.204021 0.332411

&.07097L.,

941' 85192222 S2'116309 21.159431 0.39361 8.51292 93.467991" 85

,8.46799 TotalVolume,=:

8.9 cu Aft ambient temp =

85.00 deg F.

.teperaturebof calculation =

105.00 d deg F.

1/5/'2010 11:3,6 PM:

ac8xs 0

Olein.,Ax 105

mm m

m m

ý m

m m

m A T-standard A604de S~i*

.X Y

JET WIDTH JETTEM AMB'TEM.

DELTAT

(*TC)

,deviations jTetwidth End Aea:

Volume

0 0l 0

1.4792 1193 85

-8s_..... "

1.47920 1.7*1*8 9.33539

9.33539

0.00005 3.03464 81087912 85 23: 79118 0.79861 0.670641" 0.50879 0'.20331, 8.97031 9.!19*74421" i'9.74,19

.'0.00553 3.22422 108 85 23 0.82609 0.61815 0.49826

.0.1999 6008142 10.26092 10.26088 0701245 3.46382 17 85 22 0:86364 0.54149 0.46890

.0.17269 0.09499 10.77762 10.77757", i0.01938

.1370343 1D06

85 2 1 05.90476 0.44740

' 041423, 0.13476 0.'07943 11.29433, 11.ýi29426 "0.02630.

3.94304 105 85 20 0.95000 j60

32029, 0.31573 0.07829 0'05504 11.81104 11.81095 0.03323 4.18264 104 85 19 1.00000' 0.00000.

0.00000 "0.0000 0.02023 12.32774 12.32764, 0.04015

.442225 106 85 i8 i.05556.................

'12.84445 12.84433 0.04708 4.66186 102 85

'17 1.Ii765 13.36116 13.36102 0.05401

490146 101 85

.16 :1.18750 13.87787 13.87771 0.06093

5. 14107 100 i585

1.

1.26667 14.39457 14.39440 0.06786 5138068 99 85 14 1'.35714.

14.91128 14.91109 0.07478 5.62028 98 185 13 1.46154...........

15,08733 15.08713

,0.07714 5.70192 97!.65929 85

12,65929 1.50087 15.88106 15.88063 0.10850 6.06954 97 185

.2 1,.583339 17.08498 17.084ýi A0.

5608

-6.62714 96 85 11 1.172727 18.04421 18.04317, i0.19398 7.07142

'95.20324

'985 10.20324 1.86215s 18.40951, 18.408 6..,21736 7.,24025 95 85, 10 1.90000W 20.20687 1"620 620402 0.33241 8.0709.7 94 1 85:

9 *2.1 41 21.16309 2-1. 1 59.4.31. 0.3936'1 8.51292 93.46799 85 8.46799 TotalVo m'e,,

t

i 9.3,cu'ft amblenttemp

85M0 eF

.,,,temperaturepf calc~ula1tion =

'4.00 deg F.

1/5/2010ý 11:3.6 P MCac8xl1 C61618B.Aw,104

Sm~e m

im mmi nm e m

m m m C

b MT standa~rd 193 deg EnAra Vlm S

Y JET WIDTH JETTEM AMB"EM EA T CL) deviatins, jet width 0......

.0 1479.2

'13 5

2..1.47920

.1...7..48.

9.33539 9.33539 0.00005 3.03464

108.71912-

"85

-231-79118 0:75658" 0.74692.

0.56666

'0.252-19 591984,71 9.74421 9.744219, 0.00553 3,22422 108

.85

.23 0.78ý6

070017, 0.56438.

0.25017 0.10269 10.26092 10-26088 0.01245 3.46382.

107

.85 22 0.1818

'0.63352 0.'54860 "0.23637..

.012570

'1'0.77762 10.77757 0.01938 3.70343 106 85 21 0.857,14 0.55525' 0.51408.,0:720756 0.11469

.11.294313 11.2942. 6.0.0126 30 3,.'94364 105

.85

,12 10

. P I90000 0.4 1 1904' 0:.45251.

06.16082 0,O.9109517 111.81104 181.81095,, 003323 4.18264.

104, 85 19 0;94737

03288,

.0;34385

.009286 0.06554

'12.32774 12.32764 0:04015 A.2225

'103 8518

-1.'00'00 0.o 00 0:0000~

'0 60606&

ýO,'2.O29Q 12.84445 12.84433 0.04708 4.66186

'102

'85 17 1.05882,

13.36116 13.36102.

0.05401 4..90146 10.1 "8,

16,

.1250'...

13.87787 13,87771 61 0.06093 5.14107 7100

'85 15

1. 200002 boo.

14.39457 14.394,0.06.06786

.5.38068

"'99 85 14 l.28571-14.491128 114.9110 0d:

.07478

51.62028

-98

'513 '1.3846%'___

15:.08733 15.08*13 0.07714

'5.70192, 9765929 285 1.. 65929' 1.42188"

'15.8'8106 15.88063 0.10850

6;06954 98512 1.50000 I 17.08498 17.08421 0.15608 6.'62714 96 85

.1.

1.63636.......

18.04421 18.04317 0L9398 T707142.

9520324

'85 10.20324L 13.6415

,'18'.40951

'18.40816, 0.2173 7.24025 "

95 i

b85,,,

10..

i bd

.8'o00

20.20687 '20.204. 212 0.33241 8.07097 94 85

'9 2:0oo

.1.

,,21.16309 21-15941I 3 '_0.39361 2.851292

!93.467 99 S8 51...

8.46799 Total Volume =

9*:7 cu ft iamb6ient temp 85:100 deg f.

teperature-of caculation =

103.o6 degE.

12'/.3/209 020PMClc8Blx 0

Cl61iC18&xJSxl 103

mmm*,mm m

m m

mm m

m

AT/

stan'dar d

'102 deg Edra Vlm S

X Y

JET W IDTH JET TEM' AMBV.TEM DELT AT (T CL) d.ev.

'ti on.s... je. width 0

0 0

1.4792 113 85 28 1.47920

.71848 9:33539 9.33539 0..00005 3.03464 2108.79 12 85 237.9.1, 8 0.,`T1455 0.81988ý 0.6220 0.30387 9.43968

'9.74421 9.7441*9

'0.00553

322422 108 85 23

.73913

.77754 :.62674 0:630850

'0257 1.0.26092 102688 0.01245 3468 107 85 22 047,7273ý 0.80 062184.

0.3037 0.15816 107 62....-

0.7--57"- 0.01938 3.70343 06 185

.21 080952 065009 060189 028453

.15197 4L2'9433 41129425.,,0.02630 3404105

ý85 20 0-85000 0.57012`

f<056200 0.24,806 0.137601 11.81104 11.81r 1095 0.03323 4j18264 104 85 19 0,89474 0.47165."

'0.49318 0.19103.

0:11344 12.32774 212.32764 40.04015 4,2225 103 85 18, 0.94444 0.33811:

037380 0.10974 0.07771 i12.84445 12.84433

_0.04708

.466186 102

,85 17' COO00000 0.00000:

0.

000.0 000000

'0.02835 13.36116 13.36102'

,0.05401 4r90146

0.

85 I-16 S06250 13.87787 13.8177ii 0093 514107 1,00 85 15i 1.13333 14.39457 14:39446

'0..00686

.3808 99 84 1,

1.. 214

-14ý91128 14.9 11091 0748 5.62028

ý98 8513 1.30769 15.08733 15,08713.07714 5.70192

.97.65929 85

265929 1.34289 15.88106 15.88063 0.10850 6.06954 97

.85 12 141667 "_

17.08498 17.08421 0:15608 6,62714 96 85 11 1.54545 18,04421 1'8.04317 0.19398 7.07142 95.20324 85 1.i0.20324 1.66614 18440951 18:40816 21736

7:-24025

95 85[

10 120000ý

_o.

,20-2 68ý7 2 026020

..6033241 8:g07097 19 85i 9,..

___88

_9_

'--21.16309 21.15903 "0.39361 8&251292 93.46799 851

&.4679.9 Total Vohlume ;

10b22 cU ft amnbient temp=

85.00 degF.

temnperature of caic'ulation i02 deg..f 212/3/;2009:! 0-23 PM

!iCaldi~lsx&:i02

Sm m

m mI m-m m-m m

m m

mm rT/

ýstandWr

ý94ejd6djt x

Y JET W tDTH JETTEM AMB.TEM !

DELTAIT CL devi'ti;n; End.Are..Vo.ume 0

0 0

1.4792,.

13 85ý

28.........

1.47920 1.71848.,

9.33539 9.33539 1.0.00005 3 03464 18.79 12 85 23.791 18 0.37829 1.39434 1..705783 08 886.

2 12358 9..74,21 9449 0.00553 3.22422 1..08,.85

.231 039130:.

1.36987 1.10419:'_

0.95758 0.37539 1.6092 10.26088

-ý0.01245

.343210,7:8 2049~

1372 1170 1023 0590

10.776 :2 10 7757. 0.01938 3170343

<06 85 212 0.426857 1330 177

.2 0525...

1 1.: 089 3056676

!:il9433

.2942.6

0.02630 3.94304 105.

..... 85.20 0,45000 1.26373 1.24573 3

.121882 0:60964 11.811* 4 11*"

81095 5 003323 4.18264 104

_10 85 19, 0.47368 1.22247 '.27829

.M28335 0.6,4645

~12.32774 12.32764 0.D04015 4A42225 168-8 18 0.500000 11741-

'1.3017

-Iý0 0.67538 12.84445 12.84433

,0'.04708

.66186 102 85 17 0.52941' 1.12782 131443 1.356956 0.69439 13.,36116 13.36102

', 2P.05401 4.`90146 101.

85 16 0256250*

1.07272 1.31447 1.35704, 0370117 13.87787 13.87771 0.6035.14107 100 _____85 15, 0160000 1.01077

-1.2991-1

1:32550 0.94 14.39457 14:39440 0-06786 5.38068 99

....... 85 14 0.64286.

0.94003 1.26451, 1,25583 0.66690 14.9-1128 14.91109 0.07478

5.62028 98

'____85 131 0.69231 0.85758 1.20497 1.14035 0.619,06 1-5.08733 15.08713 0,.07714 5.70192 97.65-929 85 12.6592,9 0.71094,ý 0.82603 1.17750 1.08895 0.19623

15.88106 15.88063

ý0'10850 6:06954 97 85 12 0.75000.

0.75853 1.15098

1.04046 0.84509 17.08498 17.08421 0.'15608

'6.62714 9.6 85 11 0.818 63352 1:0960.

0.86524 1.14715

>18.04421 1.. 04317

<-0.19398 7.07142

!95.:20324 85 1200324 08827, ::050096 0.8856ý3 0.;61601 0.71043

.18.40951 18.40816."021736 _

724025 95 85 10 0.900A00

-0.45904-4 0.`83090 "0.54223 0.21155 20.20687,

,0:2ý204p02 0J33241

.807097 98 851

§ 1i.006000--

0.*0ý00 0.:00000 I 0.00000

" 0:.48729 21.163091 2i`1.59431 ' 039361 l8.51292 93646799

?85 8;46799 TotaI:Volu me;-=

22,.5*cu.ft ambient tem p 85.00, de~g F.

temperature of calculation =

194.00 deg'F.

12/3/2009 10:23 PMCac8xsx9

,C~l6l,8 B~i~ls94:

mI: m mI mI m

m mI m

m m

-I m

m m

m, mI m

AT/

'standard 95,Ad0e'g-jet, Ed Area Volume "S!I

i V

':Y JET WIDTH JETTEM AMB::EM DE!TAT (I'CL) deviations width 0

0' 0L14792 113-85; 28 1-.47920 1384 9.3539

......3339 0.00005 3.03464 07912 85 23.79118

.42032....

364" "099886.

0.7836 118667896

9J421 :

9.74419 0.00553

-3.22422 1108 85

'23 0.4378 1.290677" 1.04035 0:85005

0.-33394 10216092 1.0'22608'89

-0.01245 3.46382

.17 9285

0. 5455 1d.25575 1:08743

ý0.92873 1i..77762 "1*.77757

.,0:01938 3.70343.

106

'8.5 21, 04,7619R 1.21814 1.12783 0*.99902

.0.,49804 11.29433 11.29426 0.02630, 3.94304 105 85

,20 0ý.0000' 1.17741 1.16064 1..0580

.0.5.3144 11.81104

~11'.81095 0.3334.182,64 104 85 b.19 052632 1.1330

.1.'18474 1.10,240 6

'.51 12.32774 12.32764

'0.04015 4.42225

-103

'185 18' 0.55556 1.08424 "1.19869i 1.12'851',

0'57636 12.84445 1'2.84433 o004708 4.66186 0.....

1Ui2

'85 17 0.58824 1.031'07-1.20063 1.32%16 0:58405, 13.36116

'13.36102," 0.05401

'4.90146

'101 85 16 062500 0.,96954.

1.18804 1.10854 0.57889 13.87787 13.87771 0.006093

14107

. 100 85 15 0.66667 0.90052 I i.15740 1.05211 0.5582 14.39457 14.39440

'0.06,786 5.38068 99 85 14: 0.71A29:

0.82033 1.10349-0.9563ý6 SA.'190 14.91128 14.91109 0.07478:

5.62028

98.

85

1. 3 036923 0.72438

1.0 17811

0.81362:

0.457.2'8 15.08733 15.08713, 0.07714.

5.70192

ý 97.65929 85 12.65929 0.78993 0.68674 0.97893 0.75266' 0.13'*37*87 15:88106 15.88063 0.10850 6.06954*'

97 85.

12 0.83333 0.60386 0M91628 0.65940

' 0-56040 17.08498 17.08421

'0.15608 6.62714 96.

.85 1

0.90909:.

0.43660

,0.7'2335 0.41095

, 0.6443i 18&04421 i8'.04317, Q.19398

j'7.07142 95.20324 85 'i9 0.032,4, -. 9*8*O*8 0.20060' 0.35463 0.09877"'

0.21447.

18,40951.18.408i6

.0:217361 7.24025

' 95

.85

, 1.0 0

.0..00 0.00000 0,0

.00

'0.018041 20.20687

.20.2040 b.382411 8;670971.

9 5'

Xlf1____________

21.163091 ' 21.159431 0.39361 8'.5k292 93.4679Y 859 8.467,,991 TfotialýVlume.'=ý T9;48;cufvt4 ibi~nt 'temp 85.0U

. deg F.

'temperature of calculation =

95:00 deg F.ý,

12/3/2009 10.23 PM CllBx'x9

,Caclc8B.'kIls9:<:9

M WM M M

M MM~

so M

M M

M MImM

-T/

standard 9

eg jet' S;!

X Y

JET WIDTH

.JETTEM,.

AMBEM.

DELTAT (ATCL) devia'tioi:

width E.nd Mrea' Volume 0

0 0

1.4792 113 85 28 1.47920 1.71848......

.9.33539 9.33539

'0.00005.

3.,03464.108.7912

'85 23.-79118 0.4623.6

-.24211

'0.94234*

'6974 1.27674i 19.74421 9,74419

'0.00553 3122422 108 85 23 0,478,26, 1.2,14581.

Oý'97902 0.175278

.0.2964,4 10.26092

" 0.2'6088.0'.0'1245

.3.46382 107

'85, 22.500.

1.17741 1:01959 0...

81646 6 00542 10:.77762 10.7775-7 :0.001938 13.70343 106 85 21 0.52381.

.1372*1

.05290 0.87069 0.43588

'11.29433 11.294,26.0.02630 J3.94304 105 85" 20 0155000

1. 09347 1.077,90 12521 0.46070

11.81104 1"1.8ý1095 10.03323 4.18264

ý114 85 19 0578 9 5 1.04551.

1:093,25 0.93'87'0 0.:47827 12.32774 12.32764 0.04015 4.42225 103 85

'18 0.61-111

-0.99245; 1.09721 A094552 0..48680

.12.84445 1-2.84433 0.40A.66186

ý'102 85ý%

17. -0.64706 0.9308k$

877 j988 0:48424 13.36116 13.36102 0.0"5401 4.90146

'1101.

85 16 0.68750 0.86567, 1.06076 0.88375:

0;46828

'13:.87787 13.87771

'0.06093 5.14107

'100 85 15 0.73333

0.787606

'1.01227

. 80480 _..03624 14,39457 14.39440

'0068 5.38068

`99

.85 14 0.851 0.645 0.3421 0.68546 0381 14.91128 14.91109

0.07478 5.62028

'98.

85 13 0.84615 0.57802 0.81216 0.51805 1..

031093 15.08733

.15.08713 0.07714 5'.70192 97..65929.

85.

12:65929. 0.86893 053009 0.75563

ý84

.0.08507 15.88106 15.88063 0.10850

6:06954 97 85 12 0.91667

'0.41716 0.63299

.I31469 0 30286 17.08498 17.08421 0.15608

'6.62714 961.,

85' 11 1.00000 0.00000O 0.0000 0 00,00 0.,18943 18.04421 18.04317 0.19398 7.'07142, 95.20324 85 10.20324 1.07809

,18.40951

18. 40816 0.21736 T7,24025

95.

"85, 101 1.10000,,,,,,

20.206871 20.20402 0.33241j 8J070971 i9485 191 1.22222 21.163091 21.15943 60.39361 8.51292 93146799

.85, 8A46799 Total VOlUM.E' 16.5 C~u ft:,

ambient temp =

85.00 deg F:.

temperature of calculation gr96o00 deg F.

,12/3/Z009 10:24 P.MCac8xsx9

Call18B&xlsk,'9&

mminmmmmmIIIIminm m ImmI I

! TL' standard 97 deg jet n

.. S.

X Y

JET WiDTH JETTEM' AMBTEM

, DELTAT,'(AT L):

.d.iatios width*

En...e

.0 0

0.

1.4792 113

.8 28.1.4,920 1:.741848 9.335639

0.

3539 0.00005 3.03464 108:7912 85

.23.791, 8 050439' 116997:

0.88761 ':0'61877' 10.90955 9.74421 9.74419

ý0,.00553 3.22422 108 85 23 0.52174 1.14069 *0.91946 0.66398 0.26221 10.26092 10.26088 0.01245 3146382 107

'85 22 0.54545`ý 1.10103 0.95345 0.71397 0,35600 10.77762 10,77757 0,01938 3.70343 106 85 21 057143.ý 1.05794 0.97950 0.75353, 0.37913

11.29433 11.29426 "0.02630 3.94304 105 85 b20 0.60000=

1.007

. 0.99637 0.77971',..-'

0.39612 11.81104 11.81095 0.03323 J4.8264 104

'85 19 0.63158',

0.95868 500245 0.78925 0.405j3-5 12.32774 12.32764:

0:.04015 4.42225

.103

'85 1.8' 0.66667 0.9052l 0.99558 0,77847 0.40503 128445 12:-844331

0ý04708 4.66186 102-85 17 0.70588&

0.83463 0:97274 0-4315' 0.39312 1336116 13.36102 '.'0.05401 4.90146 101

,85 16 0.75000 0.75853 0.92947 0'67852 0.36730 13.87787 13.87771 0.06093 5.14107 100

.85 1 5 0.800,0 0.66805.

0.8586,

'2 0.57902,,

0,32489 14.394571 i139440 0.06786 5.38068

99 85 14 0.85714, 0.55525,

.74690 0.43815 0.'26279 14.91128 14.91109 0.07478

.5.62028 98 85

.13.0.92308

.0.40011 0.56218 C0.24822

.0.17733 15.08733 15*.S0873 007714 5.70192

ý :97.65929 85 11'265929 0.94792 0.327065 0.4662:2 101.17071 0.0'3688 15.8806.I588063 0". 10850 6.06954.7 "85 12 i.00000, 0.00000 0.000000 0.00000

.06775 1i7.08498

-117:0821 0.15608 6.62714

.96

'85 11 1,6.099,

18.044221

X8043i7,

019398 7.07142

.95.-20324 85

'1020324 1.17610' 18.40951'

,'18:40816 0.21 736 7.24025 951.85

-1id0

,-1620000:

_._I 20.20687 2.204*02 0.33241 8.07097 94 1 85

'9 133333 21,16309

.21.159431 0.39361 8:51292 93.46799

'85 8.46799, Total Volume: =

14.7 cu ft ambieni6Kt' temp =

85.00

'degiF.

temperature of calculation. =

'97.00 deg-E,F,,

12/3/20091*0:2 2.PM clx.c caic'.SB.'xlsxli*9*

m m

mmI i

m m m m

m AT/

.standard 94?egje

,#ýgjet End Area' Vol me S*

X' JETWIiDTH JETTEM AMBTEM DELTAT (TCL) deviations width 0

0 1.4792

'113",

85 28 1.47920, 1.71848 9.33539 9.33539 0.00005 3.03464, 1 08.7912

.85.

123:79118 b0.54642 1.0942,

'0.83409 0..5s,4640 10.57,177-

.9.74421 9,74419 0053 3.22422 i08

,85 23 0.5'6522 1.,692l:

0.8ý6104 0.58229 0.307 2 10.26092 10.26088

'0.01245 3:146382

.107 i85 22 0.59091 1.02576D

.088826 0,61969.

0.31053 10.77762 10.77757

.0.01938 3:70343

1O6 85 21 0.61905 0.97936 7t90675 064575 0'32693

.11.29433 11.29426

?,,0.02630 3.94304 105

85 20 065000 0.-9282-1 0.91499ý

.065754

33671

'.181104 1,1 81095 0.03323 4.18264 104 85 1

0.68421 0:8119 0..91097 "0.65178

'0-.33827

'12i32774 12.32764 0.04015O

'4:42225 103 85 18 0'672222 0.80675 0.89191 0.62479 0.32981 12.84445 12.84433 0.004708 4.66181 102 85' 17 0.76471, 0.732489

.0:0.8536861 0.57237.

0..30929

'13.36116 13.36102

0:05401 4.90146

'101 85 6

0.81225, 0.64

'0..78965 0"8973 0.27440 13:8778'7. i. 13.87771 0.06093 5.14107 100 85 15 0:86667 0.53498

0.68759ý,

037,132

.0.22246 14*394s.

-14.39440

.0.06786

'5.38068 99 185,1 0.92857 0.38499 0..651787

.021064

0.15035 14.91"128 14.91109 0:07478 5.62028

'98 85

13, 1.00000b 0.00000

,O 00 0,00,000 0.05442 15',08733.15.08713 0,07714

5.70192

,9.65,929

'85 12.65929 1.026919i

'I5;881061 15.88063 0:010850 606954 i97 85 12 1.08333 17.08498 17.08421 10.5608

.6.62714

ý96, 85

-1 1.18182.......

18.04421 18..4317 0.619398 7.07142

95.20362 85 I0102b324, 1.27411i 18.40951 18.40816 0.21736 7!24025

.95 85

1. 1.30000dd...

L20.20687.20.20402 0:.3324i1

!8.07097

,941 85 9 1.44444

].

'21:16309.

21:15.9431

'0i3936I 8.5i292

.93.46799

,85 8&46799

'T&tal Vokime =

135 Cu ft.

ambient temp=

85.00 deg Fi, Stemperature'6f calculation =

98.00 eg F.L 12/13/2009%10.24 PM ccS~x c4clWX& 98

I-I----I I-I-I-I I-II-II--I AT/i.

standard'.996 egjet EndArea Volume S.:

X Y

JETWIDTH JETTEM; AMBTEM.

DELTAT (TC) deviations dwidth 0

.1 0..

0 492 1i3....

85 28' 1....

1.4792 1

.71848 9.3353 9.

9.33539 0.00005 3.0346(4 "1p0.7 912 85 23.79 -1,8- 0.58-8-45:

1.02981

'0.7812,8 0.4N07940 106259 03 9.74421 9.74,419 0.00553:

3.22422

ý !108.

85.

23 0.60870 0.99643 0-.80318 0.50665 0'.20156

'10.26092 10.26088

0.01245 3.46382 107 85 22 0.63636 0.95077 0.82333 0.53240 0.26844 10.77762 10.77757 0:01938 3.70343 106.85 21 0.66667 0.90052 008337.5 6.54596 0,27860 11.29'433 11:.29426

.0.02630 3.94304

105, 85, 20 0.70000

084460" 0:83257 0.54442 0.28170 11:81104 11-81095,0.03323 A,.18264 104 85 19 0.736842 0.78151 10.81720 0.524 50 0.276161 12.32774 12.2327264

0.,04015 4".42225

.103 85 18 0:77778 0.70896 :0.78380 0.48251'

,0.26016 12.84445 12.84'42380**

.,04708 466186 102.

85 17 0:82353

,.6231*5 0.72626..

'0.41426 0.23168 13:36116 13.36t02

.05401 4.90146

.101 85' 16 0.87500, 0.51678, 0.663325 0.31494 0,18839 13.87787 13,8777:1:

0.D06093

.1 S4107 100 85 15 093333 0.37146, 0'.407743

'0.17902

.0.12762 14.39457 14.39404 0.06786 5.38068

99 85 14 I*1,.000 000000

'0.0,960..o

.o000000 0.'04625

'14.91128 1'4,91109, :0.07478 5.62028 98 85 i3 1.07692.

15.08733 15.08713

.0,07714

5.70192 97.65929 85 12.65929 1.10591,_,,,

15.88106 15.8063

!0.10850 6.06954 297 85 12.16667.

17.0849*8 17.08421

'0.15608 6.62714 196 1851 1.27273,

..18.04421 18.04317

.0.19398 7.07142 95.20324 85...

10:20324 1.37211. 1I

18.409511 18.40816ý 0ý'21736 7.'24025

':95 85 10 1.40000...

202068671 20.204002 0133241 8.070971

'9 8"

9 1.55556'

ý214.16309 21.15943,

ý039361

!8.51292

!93.467,99

ý85 8,46..799, TotalVblume =

12.4,cu ft lambient temp =

85.00 deg F.

temperature of calculation =

99.00' degF.

'12/3/2009 10:25 PM'Cl1Bxs9 CallcI813.xiý,x4,0.

m m

-m--

m -

m m

AT/

standrd, 400 dg EndaAre Volume S

X___

Y JET WIDTH JET TEMý.

AMBTEM

'DELTA T

(

) deviations jet width 0

0 00 1,4792.

13 85:

28 1:.47920 1:71848.,1...

9.33539 9.33539 0.00005

-3:03464

!087912 8*5 23179118 0.63049-0.96048 l0.72868 d041703 9.96788 9.74421 9.74419 0.00553 1 3.22422 108 85 23 0.65217 0.92460 0174528 0.43624 0.17442 10:.26092 10:26088 0.01245

'3:.46382 107 8..

5 22 0.68182 0.87521i

'0.75789 '0;45113 0.22926 10.77762

10.7775'7

-0.01938 13.70343

,6.

5 02

.7 082033 I 0.75951 6.030&

023360 11.29433 1*.29426

-0.02630 3ý:94304...

85

- 20

.*7 5060-

0.75853 0,74773

_,0.43911 0.23050 11.81104 11.81,095 0Q.03323

-18264 104

$~

90797

.85

19

.00 0.2 -13 12.32774

-1232764 0.04015 4:42225 1803

-85 1

0.83333,

'0:60386 1 0 :66760 0..35005 0.19533 12.84445 12.84.433 0.04708 4:66186 102 85 17 0.88235

.0.50033 0:583i,1

'0:.267054.

0.15943

,13.36116 13.36102 0.05401 4,90146 101-

985

6 093750 035927 0.44024 0.15222 0.10832 13.87787 13.87771 0.06093

14107

.:00

-. 8 5 i

1;000000m 000000 0.00000 000000 0.03933 14:39457 14.39440 0M06786 5.38068 99 85 14 1:8.0143-

14.91128 14:.91109 0,07478

562028 98 85 13 1.15385:

15.08733 I,5 08713.0.07714 5.70192 1976599

.85 12.65929 1.18490

_._O 15.88106.... 15;88063 06.10850 6.06954.97

.85 12 1.25000.-,

17.08498 17,;.8421i 0.15608 6.62714

'96 85 11 1.36364, I8.04421, 1

317

,0.19398 7.07142 95.ý20324

.85-110.20324, 1.4701-21 18.40951 "18.408016 0'.21736 3724025.

95.85 10 1.50000, I_....

20.206871. 20.206402-1 0 33241 8.07097

94, 85,,

9 1.66667:..

21.163091 ' 21,159431 0.39361 8.5,1292 z93:467ý99 85 8.46799

~

~ ~ ~ ~

1 tot al oum 11.6 cu ft

-anbient temp=

85.0,0, de&F.:

teimperature of calculation =

100.00 deg,'F.,

121/3/2009.A0:25 (.CaC8Bxsx0 Calcl8b.Asx 100

--m m

m m

m ii(

'AVT/

standard.

i" deg

'.EndArea "Volumffe S

X!:1*i i*:

'y JET WIDTH

.JETTEM-.AMBTEM DELTAT'

(&T CL) deviations jet width 0

0

0 1.4792 113

-1.85 8_ "....

1.47920 1.7-1848',

9.33539..

.33539 0.00005 3.03464.

108.7912

.85

.23.7918 0.67252:

089076 0.67578 O35868.

9.69552 9.74421 9.744..1. 9

'd0.90553' 3.22422

.1.08 85 23 '069565

.85195 "06861 0'3737 0.14493 10.26092 10;26088

,'0.01245 3.46382 607

'85 22i:0 227 "0:798'06

.691609 03751i

. 0:19260 10.77762 10.777*7* *....;,619

.360M 343 106 85 21.0:76:90*

0.73 47 0.68280.

0.3A6*1,

.01'i9is1 11.29433 11.29426 :OQ.02630 1394304.

15 85'.

.20 0.80000.

06605 1 0.65853 0.34060.

.0:18259 11.81104~ 11.81095 0.03323' 41864 104 85 19, 0.84211 D.5"66 0.630

.0295 16_

0.164251 12.32774 12.32764 0:.04015 4.42225 103 85 18 0.88889 0.48535

-0.53659 0.22614 0.13468 12.84445 12,84433 0.04708

-4.66186 102 85 17 0.94118 0.34821, 0.40582

ý0.12935 0.09184 13.36116 13.36102 Y0.05401

.4.90146

101, 85 16 1.00000 0.00000, 0.00000 0.0000

."0.03342 13.87787 13.87771 0.06093 151107 100 85.15

.06667 14.39457 14:39440 0.06786 5:ý38068 99 8514

1. 142ý86 14.91128 14.91109 0.07478 5.62028 98 18 13 1.23077 7

15,08733 1:5.08713

'007714

.5.70192 97.65929 985 12.665929. 1.26389 15.88106 15.88063 0.1'0850

.606954 97

85.

12 1,33333 17.08498 17,08421

""0.15608 6.62714

ý96 85 11 11.454551 18.04421

, 18.043117

ý0.19398

.7.07142

.'95.20324 85 10.20324L 1.568139W:

18.40951 18.08116

0.,21736

,7.24025

.. 95 85 101 1.60000 20.206871 20:20402'1

-11332411

.79748

91 1,77778&

21.163091 21.159431

,0.39361 8.51292 93.46799 85 846,799 Total'Voldime*>*

"10.8 cu kf

,&mbieýnttemp =

85'00 deg F.

'temperature.of calculation=

101.00 deg F.

12/3/2009 10:25 PM

'ac8~~x0 YO lcl8,B,,.,xl ýx-10 1 I

At Gode Asscae we stiv to be the mos repete glblgou fAria+212440 co pne spcalzn in grun eniern an enirn ena sevies Asi

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Golder Associates Inc.

6026 NW 1st Place Gainesville, FL 32607 USA (352) 336-5600 - Phone (352) 336-6603 - Fax I

I I

I SsGolder Associates

ATTACHMENT 2 FPL St. Lucie Plant Estimated Cost of Lost Generation Due to Cooling Water Discharge Temperature Limit I

_PSL Unit 1 113°F Instantaneous Permit Limit "Case" 2005 2006 2007 2008 2009 Totals Total Hours of Power Reduction 647 493 966 377 1,135 3,618 Total MWe-Hour Losses 61,050 35,631 104,525 29,489 130,869 361,564 Total Revenue Losses

$2,591,573 $1,512,536

$4,437,086 $1,251,808

$5,555,389

$15,348,392 PSL Unit 2 113 0F Instantaneous Permit Limit "Case" 2005 2006 2007 2008 2009 Totals Total Hours of Power Reduction 647 493 966 377 1,135 3,618 Total MWe-Hour Losses 61,050 35,631 104,525 29,489 130,869 361,564 Total Revenue Losses

$2,591,573 $1,512,536 $4,437,086 $1,251,808

$5,555,389

$15,348,392 Units 1 and 2 Combined 113 0 F Instantaneous Permit Limit "Case" 2005 2006 2007 2008 2009 Totals Total Hours of Power Reduction 1,294 986 1,932 754 2,270 7,236 Total MWe-Hour Losses 122,100 71,262 209,050 58,978 261,738 723,128 Total Revenue Losses

$5,183,145 $3,025,072 $8,874,173

$2,503,616

$11,110,778

$30,696,784 Note: Assumes Cost of 1MWe-Hour Fossil Replacement of Lost Nuclear Generation = $42.45

L-2010-059, Golder Associates Inc. - Thermal Discharge Study (Bound)

Contents

Text

1.0 INTRODUCTION

SUMMARY

6.0 REFERENCES

discharge density in g/cc at 115 degF,

1.0 2280697

i 9.3,cu'ft amblenttemp

1.0 17811

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L-2010-059, Golder Associates Inc. - Thermal Discharge Study (Bound)

Text

1.0 INTRODUCTION

SUMMARY

6.0 REFERENCES

discharge density in g/cc at 115 degF,

1.0 2280697

i 9.3,cu'ft amblenttemp

1.0 17811

Navigation menu

Search