ML20127B810
| ML20127B810 | |
| Person / Time | |
|---|---|
| Site: | Shoreham File:Long Island Lighting Company icon.png |
| Issue date: | 01/05/1993 |
| From: | LONG ISLAND POWER AUTHORITY |
| To: | |
| Shared Package | |
| ML20127B797 | List: |
| References | |
| PROC-930105, NUDOCS 9301130138 | |
| Download: ML20127B810 (33) | |
Text
_.........
PLAN FOR THE PHASED DECOMMISSIONING OF THE LIQUID RADWASTE SYSTEM SHOREHAM NUCLEAR POWER STATION LONG ISLAND POWER AUTHORITY January 5, 1993 9301130138 930105 PDR ADOCK 05000322 W
Plan for The Phased Decommissioning of the Shoreham Liquid Radwaste System TABLE OF CONTENTS SECTION DESCRIPTION PAGE NO.
I INTRODUCTION 3
II SYSTEM DESCRIPTION 5
III DECOMMISSIONING PRASES 6
IV POST-DECOMMISSIONING INDUSTRIAL WASTE 15 WATER SYSTEM V
REFERENCES 16 VI ILLUSTRATIONS 17 i
I i-1 l
2
l Pian for The Phased Decommissioning of the Shoreham Liquid Radwaste System I.
INTRODUCTION The Liquid Radwaste System (011) has been identified in the Decommissioning Plan as a contaminated system which will be dismantled and removed. Per LSNRC-1859, LIPA Response 10, a description of the phased decommissioning of the Liquid Radwaste System was provided. In this response, LIPA stated that
'a phased shutdown methodology has been developed which minimizes the need for temporary equipment". LIPA also stated that " installed plant equipment will be utilized to the maximum extent possible to hold, recirculate, sample and process liquid radioactive waste water. Temporary filtration units or demineralizers will only be used in the event of equipment malfunction or during periods when installed equipment is secured for scheduled maintenance, radiological surveys or other such evolutions". A more comprehensive review of our plans for decommissioning the liquid radwaste system indicated that the use of temporary filitration units or demineralizers, as system decommissioning activities proceed, is most advantageous. LIPA intends on usino a mobile radwaste filter /demineralizer skid, as a planned evolution, to process liquid radwaste during the final stages of system decommissioning when certain equipment is secured for removal purposes. In accordance with the Decommissioning Order Condition #
3, this plan provides a detailed description for the shutdown, dismantlement, and removal of the Liquid Radwaste System and describes how liquid radwaste will continue to be processed during system decommissioning.
In addition, LSNRC-1859, LIPA Peeponse_,,1.Q, states that "the laundry drain subsystem will be decontaminated and prepared for eventual use as an industrial waste processing f acility". LIPA has subsequently determined that it would be preferable, from a schedule and cost viewpoint, to decommission the Laundry Drain Sub-system. Instead, the Regenerant Liquid and Evaporator Feed Tank subsystem and possibly other selected radwaste components will be decontaminated, modified, or replaced, to be used as the post-decommissioning Industrial Waste Water System.
LSNRC-1859, LIPA Response 10 also states that the remaining Phase 2 components will be decommissioned following the draining of the SFSP. These components may be decommissioned prior to the draining of the SFSP if the Offsite Dose Calculation Manual (ODCM) is amended to permit draining of the SFSP to the Salt Water Drain Tank.
Indirectly related to the phased decommissioning of the liquid radwaste system is the potential use of temporary filter /demineralizer equipment to maintain the quality of the water in the Spent Fuel Storage Pool (SFSP). This will facilitate removal of the Fuel Pool Clean Up (G41) System in parallel with the continued storage of the fuel assemblies in the SFSP until shipment.
3
m -_ _ - _ _ _. _ -. _
l l
Plan for_The Phased Decommissioning of the Shoreham Liquid Radwaste System Section II provides a description of the Liquid Radwaste System as it now exists and also describes how it is being operated in the current plant condition to collect, process and discharge liquid radwaste.
Section III details the phased decommissioning activities, describing in sequential order the isolation, dismantlement or decontamination, of sub-systems &nd components. The prerequisites to begin the respective phases are given, as are the temporary modifications required which will keep the system functional. Additionally, the collection, processing, sampling and discharge capabilities after completion of each of the phases is provided.
Section IV provides a description of the proposed Industrial Waste Water System which will be utilized to collect, hold, process, sample, and discharge waste water af ter the Termination Survey is completed. Portions of this new system may be placed into service prior to license termination to collect and transfer " clean" water to the radwaste system.
I I
i i
l l
l l
l 4
gr y 7 '-
M
-T
-P-
-+-
T-
-I$9W vm w
y-y y
a.
m
'eer't-P
__~___.__.____m--.
__.m Plan for The Phased Decommissioning of the Shoreham Liquid Radwaste System II.
SYSTEM DESCRIPTION b
In the current configuration, the Liquid Radwaste System can collect, process and discharge radioactive waste water collected from building floor and equipment drains. Liquid radwaste is transported f rom these collection points via the 6" floor drain header (high conductivity) or the 4" equipment drain header (low conductivity) to one of three pairs of tanks in the Radwaste Building. These tanks are the Floor Drain Collector Tanks (FDCT's) TK-061A/B; the Regenerant Liquid and Evaporator Feed Tanks (REFT's) TK-060A/B; and the Waste Collector Tanks (WCT's) TK-010A/B. Each tank has a capacity of 25,000 gallons. Each of these collection tanks has a pair of pumps which recirculate and discharge the liquid to an appropriate sub-system for processing. The sub-systems are the Waste (E-043) and the Regenerant (E-044) Evaporators, the Floor Drain Filter (FL-012),
and the Radwaste Filters (FL-014A/B) &
Demineralizers (DE-001A/B). The Evaporator Sub-system is not used. Currently, the collected liquid radwaste is only processed through the filter sub-systems. After processing, the ILquid radwaste in then sent to one of two pairs of discharge and holding tanks. These tanks are the Discharge Waste Sample Tanks (DWST's) TK-06BA/B and the Recovery Sample Tanks (RST's) TK-069A/B, Each of these tanks has a capacity of 25,000 gallons. Each tank has its own pump which re-circulates and then discharges the sampled liquid to the Condensate Storage Tank (CST), Circulating Water-Discharge Tunnel, or back to one of the sub-systems for further processing.
Normal system alignment routes the floor drain effluent ~ to one of the two FDCT's.
The equipment drain effluent is normally routed to one of the two WCT's. The third pair of liquid radwaste collection tanks are the REFT's.
j These tanks collect high conductivity chemical liquid waste resulting from the regeneration of the condensate demineralizers which are now shut down and designated for removal. These tanks have acid and caustic injection lines which permit the neutralization of the collected liquid radwaste.
Additionally, the high conductivity l iqu ir'. waste from the 6"
floor drain l
discharge header may be diverted to the REFT's should neutralization be required.
Depending upon certain conditions, the liquid waste is processed through the Floor Drain Filter or the Radwaste Filters & Domineralizers. Processed water l
1s then transferred to the DWST's or the RST's where it is recirculated, sampled and discharged to the Circulating Water Discharge Tunnel or recycled Lack to the. CST. During the discharge process, the radioactivity level is monitored by an existing radiation element (1Dil-RE-013). A high radiation level or a loss of power at the sampling panel (PNL-013) will alarm and close the waste discharge valve (AOV-158).
5 i
a -.
r.-.
e
-.n, e
P'lan for The Phased Decommisaloning of the Shoreham Liquid Radwaste System 1
III.
DECOMMISSIONING PilASES The following describes the major components and sub-systems of the Liquid Radwaste system which will be either removed or decontaminated. Existing equipment & portions of piping systems may be decontaminated and re-used in combination with new piping & coeponents for certain temporary modifications.
It also describes the prerequisites required to begin the respective phases of decommissioning, temporary modifications required to keep the remaining portions of the system f unctional, and a description of the remaining systee capabilities after completion of each of the phases.
l A.
Phase I 1.
Decomm i s s iotti no / DignLa n t l i na Ac t iv i tigg a.
Isolate and decontaminate Phase Separator Tanks TK-107 A&B, remove all associated piping and components, b.
Isolate Evaporator Sub-system. Decontaminate evaporators, remove all associated piping and components up to active system interfaces.
c.
Laundry Drain Tanks TK-020 A&B;
- pumps, piping and components will be isolated and removed back up to all interfaces with active portions of the system. This also includes the removal of the radwaste washer and dryer.
d.
Radwante Solidification System (P63); isolated only, this system is not designated as contaminated, and will not be removed.
2.
Ererequisites a.
No influent into Laundry Drains Sub-system.
3.
Iemporary Modifications a.
None.
4.
Id. quid Radwaste Processino Capabilit ies a.
With exception of the Laundry Drains Sub-system, full system process capabilities remain as described in Section II.
6 i
~,
r
3 P'lan for Ths Phased
. Decommissioning of the Shoreham Liquid Radwaste System B.
Phase IIA 1.
Decommission 1no/Dismantlina Activities l
l The following equipment will be decontaminated or removed:
a.
Turbine Building Floor Drain Sump TK-053A, along with its associated pumps, piping and components up to connection to the 4" floor drain discharge header.
b.
Turbine Building Floor Drain Sump TK-053B, along with all incoming floor drain lines, pumps, piping and components up to the interf ace with 4" line at the discharge from the Decon Area Drain Sump TK-012. Note: Turbine Building Sump Pumps and associated portions of discharge piping for TK-053 AEB will be decontaminated, if possible, and retained for future use.
c.
Decon. Area Drain Sump TK-012, along with all incoming floor drain lines, pumps, piping and components up to the interface with 6" floor drain discharge header, d.
Exposed floor drain piping in Turbine Building e.
Drywell Equipment Drain Tank TK-049, pumps, cooler, all.
piping and components up to the 4"
equipment drain discharge header f.
Reactor Building Equipment Drain Sumps TK-050 A&B, along with all incoming lines, pumps, piping and components up to the 4" equipment drain discharge header.
g.
Reactor Building Floor Drain Sump TK-056C along with all incoming floor drains, pumps, piping and components up to the 6" floor drain discharge header.
h.
Recovery Sample Tank TK-069B; pumps, piping and components will be isolated and removed up to active portions of the system.
1.
Radwaste Demineralizer DE-001B, along with all associated-piping and componente up to interfaces with active portions of the system.
j.
Discharge Waste Sample-Tank TK-068B; pumps, piping ' and components will be isolated and removed up to active portions of the system.
k.
Floor Drain Collector Tanks TK-061. A&B, pumps, influent and-effluent piping and components up to the common system connections to the Floor Drain Filter, Radwaste Filters &=
Demineralizere
<nd the Evaporator Sub-system.
I l
r
..n..
a P1an for.The Phased Decommissioning of the Shoreham Liquid Radwaste System 1.
6" floor drain discharge header from AOV-245 (located in Reactor Building) to FE-397 (located in Radwaste Building) will be isolated and desontaminated for post-decommissioning service. Note: This header may have to be partially removed to provide access for decontamination and survey activities. If it is demonstrated that this header cannot be decontaminated in a timely manner, it will be removed and replacement piping installed as needed.
Note:
Turbine Building Floor Drain Sump TK-053A will be returned to service during this phase of-decommissioning as a " clean" sub-system. Discharge will be routed to the Radwaste Equipment Drain Sump TK-071 or the Acid & Caustic Waste Sump (1P21-TK-118) via a Temporary Modification (TM). This TM will remain in ef fect until the 6" floor drain header has been decontaminated or replaced.
2.
Erereouisites a.
Mechanical decontamination (hydrolazing) and radiological survey of embedded piping is complete for Turbine Building Floor Drain Sumps TK-053 A&B and Reactor Building Floor Drain Sump TK-056C.
b.
Mechanical isolation of Low Conductivity Drain (P71) System Sumps TK-186 A&B pump discharge piping connections to 4" equipment drain discharge header complete (for item 1.1 above).
c.
No radioactive influent from the Chem. Lab (for item 1.c.
above) Notes Liquid drains from the existing Chem. Lab are directed to Decon Area Drain Sump TK-012. The entire Chem.
Lab may be relocated or a separate " hot" lab set up in a different location to prevent.the continued flow.of radwaste to Decon. Sump TK-012. This would allow the " cold" lab to remain in the existing location with a new drain line installed to direct " clean" liquid discharge to the Turbine Building Floor Drain Sump TK-053A.
d.
Appropriate Operations Procedures revised to incorporate changes to system.
l l
l l
l I
l-8
Plen for Th2 Phased Decommissioning of the Shoreham Liquid Radwaste System 3.
Install cross-tie to direct Radwaste Building Floor Drain Sump TK-054 discharge to the Radwaste Building Equipment Drain Sump TK-071.
b.
Install pump discharge piping from Turbine Building Floor Drain Sump TK-053A to Radwaste Building Equipment Drain Sump TK-071 or the Acid & Cauptic Waste Sump (IP21-TK-118).
(after completion of item 2.b above).
i c.
Install temporary drain lines from the Chem. Lab and station air compressorm to Turbine Building Floor Drain Sump TK-053A.
d.
Install temporary line from 4" radwaste equipment drain discharge header to Regenerant Liquid and Evaporator Feed Tank TK-060B. A manual isolation valve will be installed in lieu of valve AOV-284.
4.
Licuid Radwaste Proceesino Capabilities With decommissioning of the Floor Drain Collector Tanks TK-061 A&B and the 6" floor drain discharge header, all liquid waste collected in the Reactor Building, Turbine Building, and the Radwaste Building sumps will be transferred to the Waste Collector Tanks TK-010 A&B or the Regenerative Evaporative Feed Tanks TK-060 AGB via the 4" equipment drain discharge header.
This waste will be processed in the normal manner utilizing the Floor Drain Filter FL-012, the Radwaste Filters FL-014 A&B and the remaining Radwaste Domineralizer DE-001A. Processed liquid will be sampled and discharged utilizing the remaining Discharge Waste Sample Tank TK-068A and the Recovery Sample Tank TF-069A.
C.
Phase IIB i
1.
Decommissionina/Dismantlino Activities
)
The following equipment will be decontaminated or removed i
a.
Reactor Building Floor Drain Sump TK-056B, along with all
_j incoming floor drain lines, pumps, piping and components up -
to the floor drain discharge header.
i b.
Regenerant Liquid and Evaporator Feed Tanks TK-060'A&B, along with their associated pumps, piping and components up to interfaces with active portions of the system.
c.
Waste Collector Tank TK-010B, along with its associated pumps, piping and components up to interfaces with active portions of the system.
9
}
Plan for The Phased Decommissioning of the Shoreham Liquid Radwaste System d.
Discharge Waste Sample Tank TK-068A, along with its associated pump, piping and components up to active portions of the system.
e.
Radwaste Filter FL-0148, along with all associated valves, piping and componente up to interf aces with active portions of the system, f.
Floor Drain Filter FL-012, along with all associated valves, piping and componente up to interfaces with active portions of the system.
2.
Prerecuisites a,
Mechanical decontamination (hydrolazing) and radiological survey of all embedded piping is complete for Reactor Building Floor Drain Sump TK-056B.
b.
Radwaste System influent has decreased to an acceptable level for processing at a reduced capacity.
c.
Appropriate Operations Procedures revised to incorporate changes to system.
3.
'remocrary Modifications a.
Contingent - Connect the acid and caustic neutralizing lines which are currently connected to the REFT's-to the Waste Collector Tank TK-010A via a Temporary Modification.
This will provide direct neutralization capability of the Waste Collector Tank TK-010A.
4.
Licuid Radwaste Processino Canabilities Af ter completion of this phase, liquid radwaste collected by the remaining operating sumps will be sent to Waste Collector. Tank TK-010A and processed-through Radwaste ' Filter FL-014A and Demineralizer DE-001A. The processed water will be sampled and discharged utilizing _the Recovery Sample Tank TK-069A-and existing flowpaths.
After completion of this phase, the Regenerant Liquid and Evaporator' Feed Tanks TK-060-A&B will be L-decontaminate.d and the pumps, piping, and components replaced for
(
future collection and processing - of " clean" industrial - waste L
water.
10 l
l
- ~.
~
4 Plan-for The Phased
-l Decommissioning of the Shoreham Liquid Radwaste System D.
Phase IIC 1.
-Decommissionino/Dismantlino Activitles The following equipment will be decontaminated or removed a.
Reactor Building-Floor Drain Sump TK-056A, along with all incoming floor drain lines, pumps, piping and componente up to the floor drain discharge header.
b.
Drywell Floor Drain Tank TK-057, along with its associated pumps, piping and components up - to the floor drain discharge header.
c.
Radwaste Filter.FL-014A, along with all associated piping and components.
d.
Radwaste Domineralizer DE-001A, along with all associated piping and components.
e.
Spent Resin Tank TK-062, along with associated. piping, valves and components up to other system interfaces.
2.
Prerecu lo itfdg a.
Mechanical decontamination (hydrolazing) and radiological survey of influent piping (embedded drains, downcomers, etc. ) is complete for Reactor Building Floor Drain Sump TK-056A.
b.
No liquid-radwaste from Reactor Building or. Turbine Building (i.e. Termination Survey complete in all areas),
~~
~
c.
Existing Fuel Pool Clean Up (G41) System Demineralizers empty.
l d.
Appropriate operations Procedures revised to incorporate b
changes to system.
e 11 oi-
P'lon for Tha Phased l
Decommissioning of the l
Shoreham Liquid Radwaste System N'tet To f acilitate the decommissioning of the Fuel Pool Clean Up (G41) System, temporary filter /demineralizer equipment may be used to clean the water in the Spent Fuel Storage Pool (SFSP) until the nuclear fuel is removed.
e.
NRC approval received for use of mobile radwaste domineralizer/ filter equipment. Mobile equipment will meet requirements of Reg. Culde 1.143. Existing liquid radwaste system process connections specifically designed for installation of a mobile filter /demineralizer will be used.
A change to the Process Control Program (PCP) may be required to add vendor operating manual if other than currently referenced.
3.
Temporary Modificatione a.
Installation of mobile Radwaste Filter /Demineralizer equipment.
b.
Contingent - Install temporary submersible pump (s) in decontaminated Reactor Building Floor Drain Sumps.
Note: If Reactor Building Floor Drain Sump TK-056C new discharge piping installation has been completed for " clean" service, this sump may be returned to service during this phase of decommissioning.
It will temporarily discharge into the 4"
equipment drain discharge header until the 6" floor drain discharge header is ready for service.
4.
LitTuld Radwaste Processing. Capabilities After completion of this phase, liquid waste water will be collected by the operating sumps and directed to the Waste Collector Tank TK-010A via the 4"
equipment drain discharge header.
With both Radwaste Filters and Demineralizers decommissioned, a mobile filter /demineralizer will be used to process collected liquid radwaste. The mobile equipment will be connected to existing system process connections designed specifically for this purpose. The mobile filter /demineralizer will discharge the processed liquid to Recovery Sample Tank TK-069A for sampling and discharge.
l i
12
Plan for Ths Phaced Decommissioning of the Shoreham Liquid Radwaste System E.
Phase IID 1.
Decommissionino/Dismantlina Activities The following equipment will be decontaminated or removed:
Note:
The Recovery Sample Tank TK-069A and the mobile Radwaste Filter /Deminetalizer skid will be the last components removed in this phase of work; this will enable processing and discharge of water collected by means other than design flowpaths (e.g. wet vacuums, temporary pumps, etc.)
a.
Complete removal of 4" equipment drain discharge header.
h.
Radwaste Building Equipment Drain Sump TK-071, along with all incoming floor drains, pumps, piping and components up to interfaces with the remaining portions of the system.
c.
Radwaste Building Floor Drain Sump TK-054, along with all incoming floor drains, pumps, piping and components up to interfaces with the remaining portions of the system.
d.
Waste collector Tank TK-010A, along with all pumps, piping and components up to interf aces with active portions of the system.
e.
Recovery Sample Tank TK-069A, along with all remaining pumps, piping and components up to interfaces with the Demineralized. Water (P21)
System immediately before entering the discharge tunnel, f.
All remaining piping and components will be removed or decontaminated in place in preparation for the operational and termination surveys of the Radwaste Building.
2.
Prereculeites a.
Mechanical decontamination (hydrolazing) and radiological survey of all embedded drain piping is. complete for Radwaste Building Drain Sumps _TK-054 & TK-071.
b.
No liquid radwaste being discharged into Radwaste Building Drain Sumps TK-054 & TK-071.
13
Plan for Tha Phased Decommissioning of the Shoreham Liquid Radwaste System c.
All nuclear fuel has been removed from the Spent Fuel Storage Pool (SFSP). The SFSP has been drained prior to removal of the 4" equipment drain discharge header. This l
prerequisite may not be required if the Offsite Dose Calculation Manual (ODCH) is amended to permit draining of the SFSP to the Reactor Building Salt Water Drain Tank TK-190.
d.
Appropriate Operations Procedures revised to incorporate
-l changes to system j
i 3.
Temocrary Modifications 1
a.
None.
4.
Liould Radwaste Processino Canabilities With decontamination activities (hydrolazing) completed, there should be no liquid radioactive wasta streams. Af ter the Radwaste Building Floor Drain and Equipment Drain Sumps TK-054 &-TK-071 have been pumped down to Waste Collector Tank TK-010A, this water may be processed and discharged utilizing the mobile filter /demineralizer equipment and the existing sample and discharge flowpaths from the Recovery Sample Tank TK-069A. During this final phase of decommissioning, Waste Collector Tank TK-010A will be decommissioned first leaving the mobile I
filter /demineralizer equipment and the Recovery Sample Tank TK-069A for processing, sampling and discharging any liquids which may result from decontamination of Waste Collector Tank TK-010A.
These liquids may be collected from portable pumps or " wet _vace,
and pumped directly. to the Recovery Sample Tank TK-069A for process, sample and discharge. The normal discharge flowpath from the Recovery Sample _ Tank TK-069A. to the Circulating Water Discharge Tunnel will remain intact with all required components such. as radiation element 1DII-RE-013 and AOV-158 fully functional (see Section II for description of discharge flowpath). Upon process and discharge of this last batch of water, the remaining parts of the system will be dismantled and removed. The mobile Radwaste Filter /Demineralizer equipment will be broken down and shipped back to the supplier for disposal.
14
\\
I c
Plan for Tho Phased i
Decommissioning of the Shoreham Liquid Radwaste System IV.
Phase III - Post Decommissioning Industrial Waste Water System A.
Phase III completes the installation and testing of the Industrial Waste Water System.
Phase III does not involve any actual decommissioning activities. This work has been identified as a Phase of the Radwaste Decommissioning Plan for the purpose of inaintaining continuity of the overall project since this phase of work must be coordinated with decommissioning activities.
Note: Termination surveys shall be satisf actorily completed for all systems and structures in areas where liquid waste collection floor drains are returned to service.
The Industrial Waste Water System will be partially implemented via a series of Temporary Modifications as the phased decommissioning of the Liquid Radwaste System progresses. New floor drain piping & components, sump pumps and discharge piping & components, and other piping &
components associated with the collection and discharge tanks will be installed. The collection and discharge tanks are the decontaminated Regenerant Liquid and Evaporator Feed Tanks TK-060 A&B.
Final tie-ins, initial check-out, and operational tests will be completed prior to placing the entire Industrial Waste Water System in service.
15
Plan for Ths Phased Decommissioning of the' Shoreham Liquid Radwaste System V.
REFERENCES 1.
USNRC letter dated June 11, 1992 to L.M. Hill from S.W.
Brown; subject: Order Approving the Decommissioning Plan and Authorizing Decommissioning of the Shoreham Nuclear Power Station, Unit 1.
2.
Long Island Power Authority (S. Klimberg) letter LSNRC-1859 dated November 27,1991 to U.S. Nuclear Regulatory Commission (Document Control Desk); subject: Additional Informatiom in Support of the Decommissioning Plan for Shoreham.
3.
Offsite Dose Calculation Manual (ODCM) 4.
Process Control Program (PCP) 5.
Flow Diagrams, MFSK-17 (A-F) 6.
Flow Diagrams, MFSK-46 (A-D) 7.
i t
i t-16 f
i
Plan for The Phased
. Decommissioning of the Shoreham Liquid Radwaste System
~
VI.
ILLUSTRATIONS 4
1.
Figure 1 - Existing Liquid Radwaste System - Gil 2.
Figure 2 - Liquid Radwaste System After Completion of Phase I 3.
Figure 3 - Liquid Radwaste System Af ter Completion of Phase IIA j
4.
Figure 4 - Liquid Radwaste System Af ter Completion of Phase IIB 5.
Figure 5 - Liquid Radwaste System Af ter Completion of Phase IIC 6.
Figure 6 - Proposed Method of Dewatering Spent Fuel Storage Pool - Utilizing Existing Discharge Flowpath 7.
Figure 7 - Alternate Method of Dewatering Spent Fuel Storage Pool (requires change to ODCM) 8.
Figure 8 - Proposed Industrial Waste Water System Configuration i
~
i i
~
17
..=.
w h 64.-AwAA W J& h.de.J6.a s ChhpA
-A-W^m MI
--Me A MMMM#
htdh4 % M hMd J dhM S 6hJ h-4 A% 4 edb 8-J-JD4CAdAM.d-=AiNf*J4-.'Mhr.-mA4._4.iv4 M 3-4a
$-,,.U - -
--._ ? _ _,__
_.--.-...._._4.
- l'l I
l
.. "T l
- 4 tl i t '~~'
'Il 8
a b,
j!
-l -
.g i
~
t gi kma e
i
,i X
d
,Y i
~=
g i s. ej -
yl j'
l
=
a l'i L
r-ii' 1
g;g
...1.
2__
lw l
=
k it.
EQ--
.---(
qi r
I ll; Efl" II HI g.j J1 it-l g
a i n. q 1;i n.l au oll.
i I
1 0
I l
ij n-
,( ii- )_
Tn. pJ g ~
,I c
m ill I(
,,. y
_ i
,,,. g i
n.
a s.
1 f
IIII d i I [> l l
g s
g n.
icii j q-E
> Ii y c.,
b fr~
1 g n. e lft Mili a La lil pt E
t 3 l e l4 I
ll e
w w
Eg]
4 e
+
)J"35,"d w
B,j.l,r(As "3
i 3
1 i n. o ;;,
gn g n..a lh -
holi q 3yg, [,
i
)3 1 ;il a
i f
__ __ _ _ _.,s _, _ _ _ _,
5_'
6
=
,=
l l m'l_f N el lMf L
v v
s n
+ ii[j l" Q!,l Ha ois m
I i
c-ng
-er gl 1 es. -Q )
n- )
._j ; i pII I
p!_ 1 i
ET+
s a i,
- n. i i
an ii is i I
l 41-lI en
- I di in-i
.._,.-_;.__._.-._,__._.....m_,__,,,
...~-, _
r
<. 2 E. _ _L..____..L _. !
- _
l-4 i
i
_1 l
hg I I
~
p!
r7 7}----
r' l
m p; # !
g l
Ig e
p_.__-.
.J e
to l
al k(
f.gj t2
Td.__ _.. _,
?g jI P
~ ::: 1 s!=
'~~
,_ e 1
l I
"T. -
If W
g 1
- ~
r --
._.l_.
1 :
- 12;a
- m
_y t
E g
g g.
h..~
l il=.(,1 hl r-y UN
.l n
11 a
I t"
ll j f 2
2 j
N JA l j g.
l l UN r
ed E
>l
(
'T i'
f o
e r&*'-
,g5i*
f hg o
+
g Ii g j[. -Q ll..*
lt Ig Q lll Gr x
o
,8I* J-Q 2 i r.[*
E cE
{
(~
g fi IllI
{ i I C)l
+
9, g
L b
[ $1= [I ij l
~
s*
g n
h
~ ' - ~ ~ ~
( $I*
g y
c5 L
it l}
g i,
g j g..-d I!l
[B i
r 3
p,. a lh B
=
i a
v
=
=
=
q._ _ _
_ _ _ _ _ g _ _, _ _._
i "lf N
~
elf l L._ _
4 ))I I --
o.
l u
n p
Lif t
i n
H e n l[f
" =@l I i
s s e
1 l
~
q;3l
-it g) a il" 1
d i* h j g. 8 j
f l.
I ji l
l l
I
-l
~!
j 1
13
-in-ll
-en gg li ei. -g ig n
-! g en
'e ll Iu F-
-L L
l i
i 1
n 1
I
-e i
e I
w l
=
a t
~
,..,.. ~. _,, ~.,,.,
.,_-,_,,...,..,,.,.,,.,.._r
,,._,.,_..,~.m.__=..,._,....r;-
"hm.%ghm_daeJ 4.e-M.aMhd4_s4--
m.h *E m M.am.4i.,-
^ - - - - -
A_,,.4 a,
4%. hag. #4 awl n
.Am.-.., _.. -
~
.h,- - -,
[p l
q i
- qlj.
a
/':
l l
h
,e
)
i
}y
,p l
===>
r fi
- s id D
Vs I
k l!
gl
_l..
~
r._ __
-.. -.'h I r l*
-w_
4 e
2
- :1 l lll[55
-[_[it<f}["
ll 4 ll e
it g [
i 1
_[ 4i. Q
[ l'.
~
V""
l l
,W, Gd a
j><
.o - - --
, f r..g e:--
n l
~
o II j!
, tr. e IIg
~
E-i.
l ( i i - )-
i n
n I
83 IIII
{ i l C)l
+-
m e
g s
b5
% in. C ]![
I a<
s g
i il* -Q
- qI 61 s
i t,
pg n
e, y
CA 8
i! 7 p
,. h
~ [t
---a g
a l
=
I il i
,il o
i o
4
~
di8I I
~
o I
l 3
I
=
i I
i 1
45- )
r----h-"!g i
I I
i inl li '-ki]
!),
j
-{
en
's
_1, ic
=
i c
3 i
.. _ _ _..,. _ - -. _ ~. - - -
a 1
_ _. l_ _
_ _ J _ _ _[
i.
L.._,.D b
a g
m.
o g,ir i ti
---}
-r l;.
t, l
{ *'- ! [ [
i I
p;
[tp j d'
- +o i
h.
!g el
,ol ss
- t. "
g 3
- 3 y
q g.
t e i.gl, -
g q
- 1 j rl-y
--,,14, -
g
-)
[
g$
l a
i ll
- Il li--- li i g I
~
YI y
(
il
_ _' _J
[:
1 y
p..
) ;l i
I l L
e:
e "l
g6 h
l t
._._911- ---[.
_ 4_,___ 7, ( 5 i. )z-
- s o ;t.
3 g
"s fili
+{ i sp!
5 1
9 t,-
I 9
a O
c3 c
3 :z 7 2 3 2: _- =.2 2 - - ---
o
- - =
1 _
._}---
1mi' l
l i
i I
a i
1 s
b r - - --
L - E '5-l
~
I l
I sg
~q
+
il.
.I L-i
),a s
s y
l]! g i -_
p 1
~ T~
T F
7--
s m
i I
e
=
~
_A-a maiip AJ-m-
e-4--4-E.=*m A +44h--ah4h-+A=WAdA-h4__'Ja m A&W.A--ii2,---J--u-swA3M 4-M%
-MM+~h-2 4.4
-a4 a=_mah-.M AAmA
=a44_42.m&
t-u
--A.-A r
_1 j ___
n i
j
_,7
~
j r ^- {
il
{l hl ft l
l 7
~
7.1 :-
g 9,
d,,, -li a
ra 2,g it g-
~
S e
F$
L kit.lo 43._.
~ l
.9
. g.
su s i 8
n 1
l l
- M m
>i o
n u o
O
- j; 4;. a ll
~
Ob h3 c
o 55 9, t l
c a
9 n
a a
~~
_ ;_ __._ _ _ ____#=_,____,
I p - - - -c i
i
~
l 1
I L
I L [ 3]l I
~
Y I
- l-r -- - - h --
A' ll
~
1 i i i
4 l
II 51 ' - 9 III ll g.1 ig p LJ 1
l
~
t 1
N I
a 1
1 e
l
=
1
~
l
--i
~ -
A-au-----A-_4---9-e-+-.-L
-a-44uMwhe w
Aah s-he 4mJ@a..
J4-aAA.4..i.4he4,ea--,ewa.4-m-v
-.+m-,a,m-e*->a--.4et,-ma
.w--..A---a
.m su
,,m.
a 4
.A-4
-M 4
4 l.
O l
}
P=
1 f
O C
.r r
~f, u
i I
hl Il l q1 -l-
~~
m 2_-
g gg g
i t
a g
4 i;
I' L r
r n
EX l
W-HIIH
- -r l$ tl -l.
g Dll[-
Iri dE I
W!
u E
z j
a z
9
.: a l '
ll a
- b
@l o
vV K-Q it. H a
,os
![
b s
w 3
2 i
Od D i
e B.
\\u-l n
a w
V W
t S
9 7
)
a N
h 6 N h h
.gg g.
I l
N ll 1
.il u
i o
r---
I r
1 l
e l
erh l l
l
~
l i
1 llI si i
l
,i i
i wy,---
,n-w-wy v-r+y ww y,ry,--wy-yr w',-7 w
y n--.e,
--m.m a
4 e-e---,
Mum u
af wi.e-w-u.sv.
w---m-m.-
a b
I O
b E_
I
_ _ _ _ _ _ _ _ _ _ _ _ R
. s,1
\\
1
'g -l i
n i
s gy y-t--
t_
h A
l 1 l gg l
~
l e
i
_,f_
A e
l l
l f,Cl.!~
I i
li 1
n i
i:
{
l E
8 J
l x
]#
l s
r y
j
~
a l
1 l
l
( ~X i
i l
s a
i e
F i
so vy i
g l
d/m N e
u I
g; j
I
[
4 j
l 1:1 i
i
-m j
si
,o y-i
/
r o j
u l
[E G
i
/
F e
i i
s a
/-
2 0
ly
/
\\
\\
??
~
Eg I
/
I i s I
/
5"
~
d ;;
I dE
/
s$
I di g
{
w e
l I
9 J ct E
y
\\
o a
\\
l Y
\\
\\
l i
a x
I s
i I
\\
I g
I y
s
==
o s
's i
\\
l I
's i
i ggg s s oIn i
i i
s a ts i
- BEE i
=
\\
St "
l l
8 d
-~
i.
\\
/
I ig N ~_j l
d, < - - - - -. - - - - - - - - - - - - - - -
-._ d l
N I
l l
M l
e j
N
[
e L
T g
5 0
,m._
E y
li !'
j J=lyj![ Fl 1-W t_
l gu
=
h p {w $
j-g r-lQ e
g l
L i
rw,
_I a
b d
l gl[1 c
9,g
,,,: [
g u
i4 g.
3 l
8 s
l by 49
[
T
~
[
~"
o o
n
- (
er
(
U l
1 9 rh n
a f"
ei e
N
- E og a
m i
ey o
a 4.
a O
$e 5I w
w l3 m
1 m
e o
1 t"
g
?
JW cr CL O
l I,
00 J
a 9
ii
~-
u.
V O
S-a i
6-0 1
6-a
\\
q-D I
q-c I
q-o i
i 19
~
{;E a?
I
?
I
's E
5 i
i al 3
S
-g
.g ta l
ea i
f*I i
Q l'
T~
['
T i
i 1
l m
a n
~
ATTACHMENT 2 TO LSNRC-2004 Proposed Schedule For The Planned Phased Decommissioning Of The Liquid Radwaste System
m
.-.~.i.n-QEh PHASED DECOMMISSIONING 0 Authot at; H
i
_YE Alt !
190*J Al'a..
. T.
r
(,
MONT11i DEC JAN Fell MAR l 1.icensing /
nn; va-A (! #%g M ta: + 1
-A.-
}
ma(%t tewart l
c p, g.,
,,l,eTlll bllIWy t"7 W ! vt
- w > +n 't te.%=<t i 7,*" M
'W $
- l nor+t te ut ?W
',em i,..-
..-V,w w
&wumww
.__-.s_m. wo+
u
_ _ +. -.
V V,a,, k. >
tw its w m '
nem 3 Do l ()}ig i
s >w as r* -s w 6 Pe w 8-0 Id 69
- lIf(tpp( g f
j W < %U8N FO*( /** %
Ni" P' Y' '
l e m.
e n +r :,.ru l
j p..__
.. _m. r.
,,e i
-~
k u =wwt wM u
- ggg
, %m i
V y i-e.u e r piime om
~ ~, -
.-.....l..,.-.
.b __
L PHASEI PHASE IIA PHASE IIB mumED CONDmONS:
IEQUEED CONDmONS:
REQUEED CONDmONS:
)
e Mar t f, r or-en ec@ in'ipnt 1+an &
. t W.t ty no mc' d*sqn ir huent r
rt 'l0 %"r dr oss & re-ro-A* w neeftd re +wte a s r.eaia d b ' A s
NM' ab;rve ai t.f Itr IFNfir-N.* WF Y
WWW
)
!)
f u tir e B di)
LT H is+ l! topit)
Les m r
i hv ir' twt frcen Lour. cry D uins j
u - biker
- 2) e, e m y i m.m o a..~ cgq
- 1) Ny y M q & S.;r e,y of ir f hie r t i
v gy3
,.ng g,,,,
+
' t.
t,N e t e f.w w a rs. ' 6 - O' 3A kD b g;gg r/ d it - P.r*
R e teP W M k
- 3) m q. m nh k n d E C F-T-177 ( F' 71 tw) rg regian ic I for r ecreton at v
( Pr wt to T& - 051 A i B) te%ced to; M y (Pncr to l
4)to,ma% e,fwntuvs IL-C U A H.'0149) tet (Hof tn b -L12)
$) (on e s11e ty m rena u er (N52) System tw c ovete (Pm to 4 -C L 1 A 10'1 O bd E 17/14 F. 3/11and tFC)
I DCC040SCtfD ACTMTIES DCCOWSSCt#4 ACTMTES DECCMA33Ct#4 ACTMTES 1
g) e,) tail. L'w Al'OL Ah'$
9m 9) 'Pd '*b bN 'bW b M WP
- Ih bb I1NH bNANI BON
{)
wu d tsn u
"* - W A ta -W B n,,
4 o-==-
o.,mm_
m
- c. i. m n-ase
_g n m n.p g r n %, s a tm m A r.,
n+s& e c-) iAta'i 08AA 'A+.
%.rm in t.m m.u A $ep.3 + mc CZ_gt,. _ _
g) WA571 OMICD T ANK
~~
~
-Diti t a T "A
- 4) tr emto tu tts, omeFWG TF -010!4 d) " W IW Ob - 5 0 ** s trw'..;
E' 1
k h'
b (h
e.g hgy B
e) I. id fA LL f EP DMN MNK n.024 j
i f) u b;t., [we 0% t.uur h : %4 & []
jng___
(J N11 gi k APwAMI fliTLF tL-0148 t c R 7--;1; 'r nD N T N L p km tnDG nom t+AN Scur 10 M A-12/t*
4 -OtfC m
- m D T4U g r toon pm N.Tg g fe-D1; F) MC M PY Lt#PJ ' Ata
~
TDA* hCDS TEQUE)(PHAE 2 K3) i; 64:wert tw staAJ:re tt -w a cwm.nt - metu se% m e w i
g) D$CHaftX W A$f( $AME't[ 1ANR C @ectaf IN t0 (Or.r60% A'd & (@JbtA i
u-cote
-.a m.n; vert %t me c..rrentiv mm fiML enee s ta tu etns l
7e+v61A LA D i F1r Dre eC@.
i w we t s iv 1 ah itur uoos reosseo mm w True koos reounto use u i i..n.ii-ci n
i a for n-sta/s) c) vst n < rm-t-e t > d re' t wante Enq F1w gu,p i po3 d msw temp 3" he n m # Ra1.
o err su ar/so Cra n Sm (b -054). u har ge to ha s.nte erg. sac st. no (qu+ Dm n9 to tw FEFT. A i
f o r Dren he r (%-07 0 mnnt isaat on me G to hsk
}
TW vt-la 03 m ree i>r.e to seNe it,e s ave ri ne t s n = r eg tr m t w T A-* B 4 gg,g$3.m m m t
i a sca t-aivi ruz-sm st/so mp (b -U534) ta ty im. ante [pp W er h-M.u &9 m.',M Ew hm p'ter T* -v5M ( sp ete) 4 Ayn ma, -4 o.
i t
i t
4 k
1
-_....__ ___ _ _-_,,.~- - _-.- _ _
f b Gil - LIQUID RADWASTE SYSTEM t
i Iwa g y_ _ I _._J UiN _. ~!. _ J ul_.
1_A_l 'G i
_ _SEP _ I _._O_C__T NOV
}
\\
l t
b l
t t
I um p,v t+y 1
J t+y. w. I q *n - a vw $. c.1v i
t y g.e,m.t 4., i 5 y vue.une m enp(.rao l
y sw es. we v. e
... p....
y ve v m v. s _.o_ _ _ _
a-._
r
___3 Y
[
na r.
i
,,,vr -,, w f
(1st -
4& ?1) 6 k t'st_-
__7 ewstfr d.est_ _ _
r f
l cet no r-
%, n,,o
.s - !
I V
t Y
y awat tu m *.u.
_ _._y_c,ra n - es.g_
j 5*
=*
t PIIASE IIC PHASE IID PHASE III t
Ri? QUIRED CONDmONS:
REQUIRED CONDmONS:
RIQUIRED CONDmONS:
- 1) af. mm ; & smy a
.r oot
- 1) $wuma i %ey of iwe~
t) Jemneen br.ev coveto
(
d pra ir, meet te S u, p m2 is ewrree 4r sm, n
<m M mm TWA A W Lt4 & 4 --- 0 71, f
- 7) Ik ly J P un we f r orn Fi
- 7) W tq 1d Pase %te t,eing tM) or T vt w.* Uch a so a' erd to h te nt* b%
w e / t v -on
- 3) Knc apprm al recenei for Tirne Sf r f are*/Demira reg'd to ernf>ty
- 3) WP r%st t a dr y'a $ ( not t -->
C4 f bernen & decorrott C.i f nrncv ol d the. 4
("
- Hmer s p er.n o <,m tr e i. e 15 :13 mam g
- 4) NRC et rmnst to use ivrp 0;"#l**;'*V* h * * %
i fautwa sf 4 Pe rnevnf fe r Ekoi
& N4 uf tormerfsd to spiten6
- 4) ODC# thorige regutes d f
I c8 1 - nr tw T-m k ~1/1/M f 3/1S/v3 our we s - t /193 f: 4/1Uv3,.nosm r<tyist [c4 T_;is j
DCCCMOSOM ACTMTES DCCOLM331 CMC ACTMT1CS DCCOWISSOM ACTMTES t
<t) N X BLlk) fiOOH (%N lth
(,
M El Wh A.
Of d'
> g) (OMPL(M flNM T'( lM Of Th Q' E&
MAH [6LHA#l! H;A f4DNNING
$ASIf 6 AI(R Sf 5?lW g qq g
p f
b) I'If YWI.il, hf.K 4 DA NN T AN8 b) IIbEONL4 bhEIk ANO NIWP 6
4 w
Cf $ 4LT{ $47[R $YT.flW c) RADA4 W fiLitP
- t. ) 6 AM ALi[ IQuip [ MN $JMP R-014A
'T k - 0 71 c) PtKf 4 AST[ AAT[R SYUIM d) RADwASTL 14V N c) FAf W 5'l fl.M 4 P NN 7_'kW lti $[ kA(
' lif - N ! A T F - O'-4
)
e) TW M9t* 1 AM l d) *^5II CMICE" I AY i
n.m.
m
{
Tuer uoosimam (mas e) g n cm w,m w,,
I'*^
a)inste te.% % a. w e ra.</t mm b
k p d art s ptim, ( prinet t to e, sbng pp
}
4M},k' a E7 o otmei ta,r a 12 p% e ss f r c,m g i J1 to RSI. (N0ilD movt+e res pr x ed es f) M "( L8ANNG f'!PM &
.n n.. o, im mnNms m m o m em Otcan o iN ru,ct iN ene 4
C4psg
-cm cmem - inom t.
f%er$Me fivT f(p) # $6a tid R1 Ud)
TI # MIN ANf i SVWilYS Of SAM AFE Etl4 s u mps <
Nf;)hlp
%et tur y cm,,
CONT.
ste fd REi. D UPCAT[- D DAID (-[C 9,1H2
@ g.. _. _ _ _
/%
f 9-
)
_v,..-
--m-.+.r,
ATTACIIMENT 3 TO LSNRC-2004 Project Technical Description For Mobile Filtration /Demineralizer Units Pages 2 thru 6 of 9 And Associated Figures
-l
Section i PROJECT TECHfl1 CAL DESCRIPTIOf1 A.
RESPOf1SE TO SPECIFICATIOf1 In this section, DT responds to the technical specification included with UPA Inquiry flo. S.
02 0075 for a Mobile Radwaste Fitter /Demineralizer Unit.
1 DT's proposed Mobile Radwaste Filter /Demineralizer Unit (RF/DU) is designed for easy installation and demobilization. The modular components are intelconnected with cam-lok fitted hosing and piping to aid in easy assembly. The design, materials, fabrication and testing all comply with Nuclear Regulatory Guide 1.143.
The unit vessel will be pre loaded with 15 cubic feet 90 cf if h;ge;, optierT' vec^0!
chc3ca) of mixed bed (00/40 cation / anion ratio) resin. The materials supplied are nuclear grade cation (H') and anion (OH) resins for maximum decontamination of the process stream. These resins have been shown to be effective at over 20 nuclear power plants.
- 2. The Mobile RF/DU consists of the following components:
01Y DESCRIPTION 1
15 cf domineralizer equipped with pressure and interface connections 90 cf dernineralitet-eptionf4)-
2 Tri Nuclear 150 psi,125 gpm mechanical filters, parallel flow and isolable 1
Centrifugal Pump - 10 HP, close coupled, open faced 1
Suction strainer, pressure gauges and flush port 2
25' influent / effluent hoses w/2" 150# RF Flanges X cam lok 1
Piping assembly, spool pieces and instrumentation package 1
Set of sample / vent hoses and valves for unit venting and sampling 1
Set of sluice in/out hoses and suction wand for vessel reloading A detailed description of unit components begins on Pago 4. Material Safety Data Shoots for cation and anion resin may be found in Proposal Section IV.
The Mobile RF/DU is fully equipped v/ith pressure indication and interface connections.
The domineralizer vesselis hydrotested to 225 psi. The following are unit capabilities of note:
BYPASS: The Mobile RF/DU permits bypassing of; the booster pump, both, or either, of the mechanical filter (s),
the domin vessel, or any combination of booster pump, mechanical filter (s) and domin.
Th:s Document is the Conhdential Property of Diversified Technologies P 275-DT 2of9 12/04/92
. _ _ _ _ _ _. _ _ ~ ~ _. _
~
1 ISOLATIOll: The following components can be isolated while the unit is operating; the booster pump, both, or either, of the mechanical filter (s),
the domin vessel, or any combination of booster pump, mechanical filter (s) and domin.
FILTER CHANGEOUT: The mechanical filter units are equipped with isolation and bypass valves, air inlet and drain ports for blowing down and changing each filter unit while the other remains in servico, it's important to note that those filter units utilize the same inochanical filter elements used in the UF 200 and UF 600 that have boon employed throughout Shoreham's decommissioning project. The commonality of spare parts (consumables) reduces plant inventory and simplifies waste disposal.
I PRESSURE & FLOW INDICATION: Prossuro gaugos oro positioned to permit determina-tion of the pressuro diop across the strainer, booster pump, either/both mechanical filters, and IX bed during normal operations. The flow rate meter (the samo instrument utilized on the UF-260 and UF 600) will accurately indicato flow through the unit.
SYSTEM (S) COMPATIDlLITY:
Due to the commonality of system and interface components of DT's process systems, the Mobile RF/DU can be utilized in the Temporary Spent Fuol Pool Cleanup Domineralizer System (ref: LIPA Inquiry No. S-02-0076), or vice L
versa, to increaso process rates or flexibility, should futuro processing noods (either volume or DF) dictato. Given the unknown and unpredictable nature of decommissioning work, such flexibility may be an irnportant benefit.
l MANUFACTURER'S RECOMMENDATION: All resin manufacturers have a recommen-ded flow rate of 7 8 gallons por square foot of surface area of a bed. Flow rates above the rocommended levels will rosult in poor DFs for targoted isotopes, high pressuro drops l
across the IX bod (followed by even higher pressure drops as the bod compacts under l
the elevated pressure) and possiblo hydraulic damage to the resin. A 24"(15 cf) vessel I
has approximately 3.14 square feet of surface area. At 8 gpm/squaro foot (maximum recommended flow rato), the maximum flow rato for a 24" vossol is 25.12 gpm.
\\
l this operational restriction, DT offers, as an option, a 36" (30 c uso in the Mo i _ _ _. -
This vessel can process 57 are feet x 8 gpm) whilo maintaining resin manuf ac u e flow rates. Tho 24" and 36" vossols e fittings and cor
- only vessel diameter and
- 3. A P&lD of the proposed unit (DRWG:92-275) follows this page. This unit incorporates all of the valving and bypass capabilities dictated by LtPA's specification. More importantly, it also includes sampling and venting capabilities, as well as the hosing and fittings necessary for sluicing spent resin out and now rosin in when the vessel must be reloaded.
P This Document is the Confidential Property of Drversified Technologies P 275-DT 3 of 9 12/04/92 l
i.i.im. m re ma A
-AweA dkA 4E4-
's.<.h4W 4%e
- E-+-
-ma 4-Me+J.A3A
& 1A e.w
.34i=.M4 2 aD & 4i.w A hmm an--S 4--'J" h J4CA-'
n414--sh.4hmA),hmA 2ahM,,&-,A,A_,,m,a i
r l
f I
V k
J n
N c
5 t
I N
- P I
hC
' \\
r
- a yg t
. /
- j"
- (
3 a
e
.-y_
\\
s
/
- ed ' =$
I, K
L r
t
,J O
-\\
i p
=
]<
~~-
+
I' i
88 e.wil..
2
,9
(
C
~
J~'
C-
,t
/.
j h
85 1"
I l
i t,,
I-I. _a.__t P
era f
me 4
I s
g a
n
=7._'
- _.p..,,, p -.
g.
g.-
M n
e i
I a
- [
, *+-
I w,-.=
i
}
- j%
,--e g
h e.
s e
3
(
M it
'"(<.j
- a, :[,*- - -
- - - - - +
J, j
si
?
- a w 'e f
U.i nb t'
a I.
I i
l s
<4 x_4 7.
~
b[/
l 9
f ag 4,
r,h 3
'es
' t I
~.~.... -,-.-..-.. -. - - - -, -. - -. - ~ - -.
-- - -~..~~ m
m-
B.
DESCRIPTIOfJ OF UtilT COMPOilEf1TS Major components of the Mobilo RF/DU are described below:
15 cf Venel-t-
The officiency of ion exchango and filtration is directly related to vessel design. To assuto optimum performanco, DT has designed pressure vessels with the characteristic of uniform plug-flow of the process water, that allow comploto removal of spent media during sluicing.
316SS Johnson screens (a standard-setter for the filtration industry) are arrayed to provido rnaximum flow rates with minimum pressure drops.
To reduce the number of throadod connections subject to leaking, top ponotrations, including the influent and offluent ports, are wolded cam loks instead of threaded fittings or flangos.
DT's 15 cf vessel accommodatos a wido rango of process media, flow ratos and processing configurations. Its small diamotor permits it to bo installed in unusual, out of the way location.
Holght 72" Width 24" Volumo 15 cf usable Wolght 800# ompty,2500# water-filled Wettod Surfaces 304/316SS i'
Vossel Shell 304/316SS Specs
, ASME Soc. Vill Codo Stamped & Nat'l Board Registered 0 cLWm] OPTIOf4AL DT's 30 e s Iis designed to the same specifications as tho 15 c
., s ol.
Hoight 74" Width 36" Volums 30 cf usabi Weight 1
mpty,3000# water-Wotted Surfaces 4/316SS s
VossolSf 304/316SS S3 ASME Soc. Vill Code Stamped & Nat'l Board Rogu d
\\
Mechanical Filtors Mechanical fittor accepts insido-loading ploated paper elomont to filter the process stream to between 1 and 30 microns, depending on filter element solocted. SS clad load annulus shloid has hinged top for. quick clomont changos is availabio as an option.
This Document is the Confidential Property.
of Diversiried Technologies.
' P 275-DT 4 of 9 12/04/92
,_._._____a_..__..______;_______.-
l Holght 40" Width 8"
Volumo 1 cf usable Wolght 70# ompty,200# water filled Wotted Surfacos 304/310SS Vessel Shell 304/310SS Spocs ANSI 931.1, ASME IX Centrifugal Pump A 10 HP contrifugal pump assures proper process pressures and flow ratos. This skid-mounted pump is protected by a low-pressure cutoff switch to p.0 vent cavitation or burnout.
All electronic controls, connections and piping fittings are provided. Electrical hookup requires a 3 pig tall load.
Height 15" Length 27" Depth 15" Weight 275#
Material Caso Iron and Bronze Electric 440V,3 phase,20 amp Design 150 PSIG (225 PSIG Hydro)
Suction Strainer. Pressure Gauges & Flush Port An Inlino suction strainer provents ingestion of pump damaging solids. The stralner is equipped with a flushing port. Pressuro gauges and flow instrumentation have boon selected for rollability and ruggedness. The flow instrumentation is the samo as used on the Tri Nuclear UF 260 and UF-600 underwater filters presently being used at Shoreham.
liqgs Custom fabricated, hydro tested (in accordance with NuRog. Guido 1.143) hosing is supplied, including the appropriate terminal fittings (flanges, reducers and cam-loks for quick assembly and installation of the process unit.
L Material Wire Reinforced Polyester Carcass Design 300 PSIG WP Material Suction Hose with PVC Carcass - same hoso as sup-Design plied with Underwater Filters 100 PSIG WP This Document is the Confidential property of Diversiried Technologies P-275-DT 5 of 9 12/04/92 n.-~-.
,.--.----.-o-,,~.e-,
-e,
,,,-c.,,,,,
, -- m
_r_-n,m
-v,--
-,,,,--,,,-wr
.. _ _.... __.... _ ~.... - _. _
s.
s.
l DPIQ93S.Mfltd/JpgQlBogM & Instruinentation Packagg isolation or bypassing of individual vessels is provided by the valving 3ssemblics. Their status can be visually rnonitored frorn a distance to rninimizo personnel exposure. All necessary ports, fittings and access points for tocharging vessols with noW media is also provided.
Holght 15" Weight 25#
Material 304SS Design 150 PSIG (225 PSIG Hydro)
Specs ANSI B31.1, ASME IX j
Sugtion Wand i
A specially-designed conduit to aid in suctioning now rnodia from the shipping containers into the process vossol during vessel rocharging is provided as part of the unit package.
t l.
1 l
c l
l This Document is the Contdential Property of Diversifmd Technologies.
P-275-DT 6 of 9 12/04/92
-<#,4
..,*--..y...,
.m,.
---,...,-_y.-,,,~,
,*.<m.-
...:.y-,...~,
--