ML17339B217

Sys Flow Diagram:Condensate Polishing Demineralizer Sys.

ML17339B217
Person / Time
Site:	Turkey Point
Issue date:	05/02/1980
From:	BECHTEL GROUP, INC.
To:	FLORIDA POWER & LIGHT CO.
Shared Package
ML17339B216	List: ML17339B215 ML17339B217 ML17339B218
References
5177-088-M-2, 5177-88-M-2, NUDOCS 8007280551
Download: ML17339B217 (18)

Text

~

~

~ ~

S ~

~ o i

~ \

~ ,

I I I le

'I too u a ~ ~ ~ 0 MWWWM

&~i 5KEtl PrX%l@Z'+ii7'~~>

~ms- ggggg ESNE~ ESH53INK%BE~

~ ~ ' ~ ~ s ~

pgL ~

~ '

s ~

r

~I O 0 c 0 a'R 0 TABLE OF CO?PZENTS Cl O

a~ e

,O e

1.0 FUNCTION C

E 2.0 DESIGN BASES Cll

~ ll C e 2.1 SAFETY DESIGN BASIS ce O. C e eA ~

2.2 POWER GENERATION DESIGN BASIS O

0e c

2.3 CODES AND STANDARDS O

O 3- 0 DESCRIPTION e

C O

a 3.1 GENERAL DESCRIPTION O

c 'O 3.2 SYSTEM OPERATION e

O E O Q 3.3 COMPONENT DESCRIPTION e

e ~0 e

4.0 UNRESOLVED MATTERS E

e O.

5.0 REFERENCES

~l O a

I le ill 'O I ~l E

QJ CQ e O

r O.

SL e O

X CL o e

e a 40

~l

'O e

O

~P JC C e

~ l el C

~l a 0

'O ae O.

e Oe E e O IJ O

'O 0

CL NUMBER SYSTEM DESCRIPTION 5177-088-M-1

~yfl 'ONDENSATE POLISHING SHEET 2

OF 17 gf DEMINERALIZER SYSTEM es es DATE O

TSO Q4

~> IP O O 0

'7 1.0 FUNCTION Cl a

1.1 The condensate polishing demineralizer system tO c4) purifies the condensate by filtration and demineralization to provide high quality condensate water to Turkey Point Units 3 and 4 steam generators. When in use, the C7l

~ 0 c system treats full condensate flow discharged from the condensate pumps. The system is

~7

~I also operated during feedwater recirculation C%

D C OP

~0 C and secondary system wet layup operation.

0CP O

C 1.2 In addition to the filter/demineralizers, the O condensate polishing demineralizer system S7

~7 includes precoat and spent resin handling C

~0 subsystems. The precoat subsystem is used 0 to evenly distribute, powdered resins across

'Cl 4l the resin retention elements within the Hl

~i filter/demineralizers. The spent resin handling fO E

a subsystem is used to transfer exhausted resins out O O, aw of the filter/demineralizers and provides a means to discard the exhausted resins.

E CL 2.0 DESIGN BASES C

10 I

~ 0 2.1 SAFETY DESIGN BASIS Ul

~l The condensate polishing demineralizer system CP E is not safety related and has no. safety design QJ CO a basis. The system is designed to Quality, O

c Group D as defined in Reg. Guide 1.26.

a CL Cl O IJ O.

2.2 POWER GENERATION DESIGN BASIS X r CL O a 'a A. The system is designed to filter and o demineralize the condensate at. a normal 0 operating flow rate of 13,880 gpm and

'a normal operating temperature of 108.7 F 04J with a maximum temperature of 140 F.

'cCS X

'D a The condensate polishing demineralizer

~0

~I D r. system is designed to treat the conden-Ct O sate at a normal operating flow rate of D 13,880 gpm2with flow rate not exceeding c

a0 3-5 gpm/ft of ion exchange bed area.

IJ

~I E 'a ~I

~ J lJ O

'D 'D 0

CL NUMBER 5177-088-M<<l SYSTEM DESCRIPTION SHEET OF CONDENSATE POLISHING 3 Pl Ol DEMINERALIZER SYSTEM 'ATE ec 'T P 0 O

lU

Q O C

0 S7 C. The condensate polishing demineralizer Cl b system is designed to maintain required o effluent quality during normal operation, lO a startup operation and .condenser leak C

4) conditions. The performance require-ments under each operating condition Cl Cl E

Ch are described below:

~ 0 aC7 '

~A

~> 1. Startup Operation X

Cl

~ II c A

0%J Constituent Influent, b Effluent, b Cl O

c Total Solids 500-10,000 250 O Iron (as Fe) 2,000 100

~I Silica (as SiO) 500 25 C

C pH 9.1-9.6 9.1-9.6 0

a C

~Q

2. Normal Operation 0Ol O O E

~7 Constituent Influent, b Effluent, b-Cl

~0 Total solids 100 10 max.

E a Iron (as Fe) 20 5 max.

~I Sodium (as Na) 25 1.0 max.

a Silica (as SiO) 25 10 max.

C) a

~ 0 pH 9.1-9.6 9.1-9.6 Cation Conductivity 0.1 W 'o 3 (micromho/cm)

I a W

E' 3. Condenser Leak Operation C)

O Condenser Leakage Criteria CL ~ 7 0 1) Allowable l'eakage based on CL Ol Cl O

X unit operation for one hour:

a a

~1 The condensate polishing 0 demineralizer system is

'D

~I designed to allow 0.15 gpm 0tP maximum continuous condenser C aX leakage without. exceeding CD 0.15 ppm chloride in the

'aa aC steam generators.

a O lO C ~7 CL O

a

~7 IJ E 'ea CJ

~J D

~0 0 CL

~0 NUMBER 5177-088-M-l

" ~gL SYSTEM DESCRIPTION SHEET OF r

CONDENSATE POLISHING 4 17 cv DEMINERALIZER SYSTEM DATE TPO

~ ~v Cl 0

CI

2) Allowable leakage based on 0

I unit continuous operation:

unit is designed to C7 r.

~l The 4l a operate continuously under E a maximum continuous con-Cp 4l denser tube leakage rate .

Cll

~P of 0.0l gpm without ex-D ceeding 0.15 chloride in the steam ppm gA C generators.

W g

'D 0 V D. The condensate polishing demineralizer c0 R

a0 system is designed for the pressure drop,

~

0 ~

from system inlet to system outlet, not Cl to exceed 13 psi with resin in clean g

C condition, and 26 psi with resin dirty.

~ y Cl E. DELETED r E 0~ %

~I O

Q.

0 p I

4 Lll ~e uQJ E CD e

p g'C

~

~ I Q.

Cl a Or In case of primary to secondary leakage, the system O cJ

~ X may be isolated by the operator upon receipt of a a~ a high radiation alarm from steam, generator blowdown I

e line. The main bypass valve can be opened to allow O

< o normal operation of the plant.

O Cl The precoat subsystem is designed to C

X 0

deliver powdered resin in a slurry form to the surface of the precoat retention

'U ac media in the filter/demineralizer vessel S ~0 R

to provide a uniform distribution of the D

resin on the retention media.

~ 0 0M aC Ew M

0 NUMBER 5177-088-M-l SYSTEM DESCRXPTXON CF SHEET OF r

ggC" CONDENSATE POLISHING IV 0/ DEMXNERALIZER SYSTEM DATE ee Cl TPO Ql

O 4>

0 g a 0 g Sa .The precoat subsystem is designed to use a S

mixture of powdered cation and anion resins in a ratio ranging from 3 cation/1 anion to

~

S~ S 1 cation/1 anion. The subsystem is designed c to precoat the filter/demineralizer vessels E S with powdered resins at a resin loading of 0.2 lb/ft (dry weight). The subsystem. is CP <

0!

D)

~ a Ot designed to precoat one filter/deminerali.zer O vessel to the maximum resin loading, of approxi-a<<

4 X C ga mately 300 lb. dry weight, in one cycle of O

~

C 0lP operation.

e 0 V

~ 0 0 e The spent resin handling subsystem .is designed C A C

to (1) process the backwashed resin slurry, 0

discharged from the filter/demineralizer vessel, (2) prepare the resin slurry in a E

concentrated form in a range of 30-50 percent O aS (by wei.ght) for, disposal.

~ I O

D D E ~

~

e ~

a The condensate polishing demineralizer system D g is unitized, one for Unit 3 and one for Unit 4.

I- e llJ The system 'is designed to process full X

u E condensate flow of 13,880 gpm.

lQ o

'O 0

S E

a0a a K. The system is designed to assure that all

~ X vessels which are in service share the flow a c) equally.

O Ol e Ol a

D a 0 ~ L. Deleted I

O clO M. Deleted w 'o0

, IQ C O Em Ll 0

~ o NUMBER 5177-088-M-1 SHEET OF SYSTEM DESCRIPTION 6 17 C4 CONDENSATE POI ISHING DATE TPO DEMINERALIZER SYSTEM O

QJ

'k

, 4> Cl

'O O a

J5 C7 N. The system is designed for normal power

'0 operation. In case of loss of power, the bypass tO 0) valve will open.

go Cl Ol

0. Shielding is not provided.

P. The system component, piping, valves, C etc., is constructed of carbon steel.

The vessel in contact with ion exchange Ol w

D IA 7C Ol C resin is provided with lining.

C 0CJ 2.3 Codes and Standards O Cl O The condensate polishing demineralizer system

'Cl is designed and constructed in accordance with C

S a the following codes and standards:

D aC.'

0 ~I American Society for Testing and Materials

~I (ASTM)

E t4 ~ 7 O CL 47 American National Standards Institute (ANSI)

~l E

a ASME Boiler and Pressure Vessel Code

~I tL Section II Material Specifications r

~4 Section VIII Division 1 Pressure I

Vessels Ill Section IX Welding Qualifications

~I UJ E Hydraulic Institute (HI)

SD ~l O

E National Electrical Manufacturers Association (NEMA)

Q.

CL C7 CL EP X

a Institute of Electrical and Electronic Engineers Ol

~ t (IEEE)

~l 0 Occupational Safety and Health Act Regulations

'a (OSHA)

O O

eCS X e Uniform Building Code (UBC)

'D ~)

Cl C

~ 0 American Petroleum Institute (API) 0 a 'a

'e D

American Institute of Steel Construction 0

(AISC)

EP E ~I CP

~ Steel Structures Painting Council (SSPC)

CJ D

0 W

NUMBER 5177-088-M-1 ggL, SYSTEM DESCRIPTION SHEET OF ggc": CONDENSATE POLISHING 7 tV DEMINERALIZER SYSTEM DATE 04 TPO 0

UJ

, ~

Antifriction Bearing Manufacturers Association

{AFBMA)

Instrument Society of America (ISA)

Florida Industrial Commission Department of Industrial Safety South Florida Building Code

3.0 DESCRIPTION

3.1 General Description The condensate polishing demineralizer system is a four vessel, powdered ion exchange resin J2 system. The system, as shown on PSIDs

'a 5177-088-N-3 and 4, consists of the foll'owing E

subsystems:

a 4>

Filter/demineralizer Precoat Spent Resin Handling

~ Q.

A. The filter/demineralizer subsystem consists 41 of four condensate filter/demineralizer EO vessels, each with an individual hold.,

Lll 'D pump, and an individual flow control

~ valve. The filter/demineralizer vessels lU E contain the resin and/or filter media.

The hold pumps maintain the minimum

'D 0 condensate flow that is reguired for 5 proper resin and/or filter media reten-0 tion. The individual hold pump loop CL, X

for each vessel can be isolated from the 0 'Q Ct main condensate system. The flow control valves 'for the subsystem maintain an even .

0 distribution of the condensate flow through a +0 all on line units. All four filter/demin-O ~

eralizer units are piped in parallel.

X The precoat subsystem is used to place resin a

or filter media charges into the filter/

~A Cl

'O c IO demineralizer vessels. This subsystem

'c '0 consists of precoat tank and precoat pump . The precoat tank is provided C

ICI 0

with agitator to assure proper mixture Ew0 CJ of resin or filter med'ia slurries.

O 0

NUMBER 51 7 7-0 8 8-M-1 SYSTEM DESCRIPTION

'Cf pl SHEET OF CONDENSATE POLISHING 8 S(G DEMINERALIZER SYSTEM DATE CV O

yPO UJ

4 0 0 t 0

~

The precoat tank holds the resin mixture T

0 for precoating the filter/demineralizer

~ l 4 unit t The spent resin handling subsystem consists of Mott

.4 E

4O

<< PHP filter system and pressure dewatering filter system.

Each system can be operated individually for batch hl 4 operation. The pressure dewatering filter system is 4 C4 to retain larger powdex -particles;while.<he~tt PHP lc 4 filter is to retain smaller particles that the pressure

~

t0 dewatering filter system is unable to retain.

0 04

~

D D

4 r

t0 4 4

o E O

0 a 4 3.2 System Operation E 4 A. Filter/Demineralizer Operation a The condensate polishing demineralizer O

system includes four filter/demineralizer I

vessels. Three vessels in parallel are III ~ normally used at the design flow rate.

I e At lower flow rates either one, two, or u

III E three units may be used. The flow control l

'n valves for the system automatically divide

~

0 t the flow among the units in service. The

~ Al master controllers for these valves may a0 0, 4 be switched to obtain either the lowest, a r4 total system differential pressure possible, C

e ~ or a constant system differential pressure; O

at the operator's discretion.

O O During normal operation the condensate will 0uC he pumped from the condenser hotwell hy I, 4 the condensate pumps, through the demineralizer prior to entering the air filter/

D

~0 O

r ejector inter- and after-condensers and O 0 the main turbine gland seal condenser.

t4 .e Condensate 1'caving the filter/demineral-izers will pass through five stages of t 0II feedwater heaters. From there, the steam Ew4 V

0 Vl 0 4a NUMBER 51 7 7- 0 8 8-M-l EL SYSTEM DESCRIPTION SHEET OF gfC CONDENSATE POLISHING 9 IlI DEMINERALIZER SYSTEM DATE Ci TPO Ikl

0 O~

0 c

~ =.

R generator feed pumps deliver the water 9 through the high-pressure feedwater heaters R

and then to the shell side 'of the steam 0 generators.

During secondary system wet layup operation, Cl OP the wet layup flow is passing through the R condensate polishing system at a flow rate Ot W

O of 1000 gpm. One or two filter/demineral-a Q

gyl c~

izers will be in service.

c

~

O 00 When any one of the filter/demineralizer R

0 c0 vessels is exhausted, as determined by

~

0

~

either total volume throughput high conductivity, high differential pressure, c0 c

R or high sodium content in the effluent, S an alarm is given. Upon the annunciation R of this alarm, or after the maximum rec-ommended vessel run length has been c E attained, the standby filter/demineralizer 0 a vessel is put in service by remote manual push button, and the exhausted filter/

R

~1 O

demineralizer vessel is removed from E R R .~ service. Supervisory control is provided O.

by the automatic vessel mode controllers.

< c All vessel control and service mode R selection will be from the condensate lIJ ~e polishing demineralizer system control panel. The system influent, effluent, u

Ill E and bypass valves are remotely operated

~e e

R from this control panel.

0 c

At the operator's discretion the exhausted a

O. o 9 V vessel can be either placed in the "hold" a

~ X mode for testing to confirm exhaustion, backwashed and left clean without a pre-R 4

a e coat, or backwashed, precoated, and R 0 placed in the "hold" position as a 0 standby.

00 Z7 Precoat Operation O'.

c e

~I D

0 0 In the precoat subsystem, resin is man-R R ually loaded into the precoat tank where M '0R R

it is mixed with demineralized water from the backwash pump discharge. From the cD O M precoat pump the resin slurry flows to E~R a filter/demineralizer vessel. The resin 0

V is retained on the resin retention media NUMBER SYSTEM DESCRIPTION 5177-088-M-1 CONDENSATE POLISHING SHEET OF DEMINERALIZER SYSTEM 10 Pl n DATE TPO 0QJ

e o 0 0 C

0 inside the unit by the flow through it, O and the water from the slurry returns to the precoat pump suction combined with the cb incoming resin slurry from the precoat 0o tank, returned to the filter/demineralizer

.E-oo unit.

a o The precoat operation is terminated by

~0 o gy a timer set at a predetermined time, x o' which is determined during initial startup based on completion of the resin injection 0 00 a

and indicated by clarity of the water in 0 Co

~ e the precoat tank.

0 C. Spent Resin Handling Subsystem Operation o C 0 a 0 d resin handling subsystem consists of Mott The spent o PHP filter system (PHPS) and Pressure Dewatering c E Filter System (PDFS) ~

0 0.o o~ 0 The Subsystem arrangement is shown in P&ID 5177-088-M5.

O a

E a After the resin slurry has been collected in the

~

a 0.4 backwash receiver tank from the F/D vessel, the PDFS o is actuated to transfer the slurry into the top of the I

a filter media. The clean liquid returns to the receiver a tank while the filter cake (30-50% dry wt. resin) is Ill '0

~ collected in the Tote Box for disposal.

uUJ 'E The PHP system will be initiated either prior to or

~e 0

D immediately after the termination of the PDPS operation.

C This system is to retain the smaller size resin particles e 0, the PDPS is unable to retain. The PHP vessel houses the O oQ 0~ X filter elements constructed of porous stainless steel CL o a ~ (Porous size as small as 0.5 m). The filter is capable D

~

oo of retaining all the 200-400 mesh resin (74-47 micron).

e 0 The resin retained on the element will be backwashed, discharged to the receiver 'tank and eventually collected 00 D o

in the PDFS in the subsequent filtration operation.

x

'0O C e a0

'T) '0 o

a C 0 E~o 0 v

~w '00 BN F488-M-1

'" ~yfL ggC SYSTEM DESCRIPTION CONDENSATE POLISHING DEMINERALIZER SYSTEM SHEET ll OF fV DATE ee Cl TP0.

QJ

3.3 Component Description ()acr, UnH. g Filter/Demineralizer Vessels (3T66A, B C & D'T66A B C & D) a

1. Quantity 4

2. Type Vertical, cylindrical

3. Active ion exchange area when c

CII 4 precoated Maximum recommended flow rate 1500 ft 3.5 gpm/ft, C 5. Minimum flow rate for resin

~I

~A C retention (Later) gpm/ft I D Cl

6. Shell material /Size CS/28". g.~.7.'.-10" St.

D 7. Lining material 2'lasite

e. Number of filter elements

. 715S D 9. Element O.D./spacing between ca C elements 2/1 inch/inch

~C Sl 10. Length of element, 70 inch D 11. Vessel design pressure/temperature '545/600 psig/F

12. Vessel weight, empty/operating 16,000/33 000 lbs/lbs g E 13. Code ASME VIII, Div. 1 a 14. Location Outdoor D a

~ A

15. Manufacturer Graver i

E- Hold B. Pumps (3P86A, B, C & D; 4P86A, 3, C & D) a a p a 1. Quantity I

2. Type Horizontal, centri fugal w~D V

3. Total capacity/TDH/NPSH, gpm/f t/ft u 'E design 'l65/60/(Later) w C

shuto ff 0/72/NA 0

a V

~

aO E

D 4

5.

NPSH Fluid available at leg Spm {Later)

Condensate ft II

~

a X 0 6. Design pressure ,545...,. ps>g V

a m C D 7,'. Design temperature 200 F BHP at design

~

0 8. 2 '

'+. 0 9. Material:Casing/Impeller Cast Steel/SS

10. Design Hydraulic Institute

~I ll. .Pump motor characteristics IC 46OV, 3g eOHZ a classification .NBA. 3 Insulation

'U ~I c 12. Total weight (Eater) lbs

13. Location Outdoor c

14. Manufacturer (Later)

~O O

E wD

'IJ IJ

~O 'O NUMBER SYSTEM DESCRIPTION 5177-088-M-1 CONDENSATE POLISHING SHEET OF 12 17 g(C", DEMINERALIZER SYSTEM DATE es TPO C

w

a. C o

C 0,

8 ~

~~ C. Backwash PumP (3PSSA, 4PSSA)

Q

1. Quantity r 2. Type Horizontal, centri fugal a

3. Total capacity/TDH/NPSH, gpm/ft/ft E-

~

Cl

0) design 375/60/Later C7l

~ o shutoff 0/72/NA O

a Q

xCl gg c

4 5.

NPSH available Fluid (Later)

Condensate ft 0CJ 6.

~

Design pressure 150 psig 0 4 Q 7. Design temperature (Later) F BHP at design

~

0 8. 7 1 a 9. Material: Gasbag/Impeller Ductile Iron/S.S.

C"

10. Design Standard Hydraulic Institute

11. Pump motor a characteristics .46OV 36 60HZ classification NEMA B Insulation gy

~

E

12. Total weight (Later) lbs 0D 13. Location ~

Outdoor 5

4 14. Manufacturer (Later)

E m Q,

D- De let ed e l=

I

~ 0 Ill ~

a T

u E Ql '

~0 re C

~ oe O

ao a

a 0 O ag

~

0M S7 I, e

'Q c

'U 'Q I O O

O u E~~I M Cl O

O a

NUMBER SYSTEM DESCRIPTION 5177-088-M-1 gfG

~yfL CONDENSATE POLISHING DEMINERALIZER SYSTEM SHEET

. 13'7. OF DATE Tlo

o

~+0 D 0

r. 0 J2'

~,~ A E. Precoat 'Tank (3T67, 4T67)

~ e 0

1. Quant,ity 1 CD 2 Type Vertical, cylindrical 4P

3. Design pressure Atmospheric Design temperature. (Later) F 0 5. Capacity (Z,ater) gal Ol

~)

6. Tank material/Size CS/60" g x 5'-0" High a 7. Lining material Plasite 7155 Q ~C 8. Weight, empty/operating (Later) lbs/(Later) lbs OI C)

9. Agitator motor HP

~

D V 0 10. Code API-650 as design guide R e 0 00 11. Location Indoor S7

12. Manufacturer (Later) c cR F. Precoat Pumps (3p87, 4p87) 0

~c Al 1. Quantity g 1

2. Type Horizontal, centrifugal O

Fo 0 CL a 0A

3. Total capacity/TDH/NPSH, gpm/f t/ft 0 ~

design 1940/60/Later e a shutoff '0/75/NA o .~

~

Q, r

4.

5.

NPSH available Fluid (Later}

Condensate ft

6. Design pressure 150 psig QJ ~o 7. Design temperature (Later) F

8. BHP at design 33 '

u llJ E 9. Material: Casing/Impeller Ductile Iron/SS R a C

10. Design Hydraulic Institute

11. motor standard'ump

~s 9

c 5 OS a

characteristics 460V 35 60 HZ e

0 classification HEM' Insulation a X a 12. Total weight (Later) lbs e ~

SV 0 13. Zocation Indoor Q 14. Manufacturer (Later) 0 O O G. Air Surge Reservoir (3T68~ 4T68) 0IP ~

1. Quantity 1 5, e 2. Type Vertical, cylindrical

'DD gp C

3. Design pressure . 125 Psig lO Design temperature 110 F

5. Capacity (Later) gal

~ 0 o

6. Tank material CS/96" 5 x 10'-0" St.

C 0M 7. Weight, empty/operating (Later) lbs/(Later) lbs EnO e. .. Code ASME SECT, VIII~ Div 1

~O 'D Cl

9. Location Outdoor O 10. Manufacturer (Latei)

NUMBER SYSTEM DESCRIPTION 5177-088-M-1 CONDENSATE POLISHING SHEET OF DEMINERALIZER SYSTEM DATE TPO

0 O 1! through N. tog u

S 0 a

a

~

C 0 L

a D

S a E

aa a aS a S a

S o 00 0 a ou 0 o O. Backwash Receiver 'Tank S

S a 0 C S

l. Quantity 2o Type Vertical, cylindrical

3. Design xessure Atmospheric

4. Design temperature 200F e~ u 5. Capacity 10,000 gallons a 6. Tank aterial CS

7. Lining material Platsite 7155

'e 0. 8. Size 1'44gg y > 13> Og'igh a '0S X 9~ Weight, empty / operating {Later)

10. Code API-650 as design guide ll. Location Outdoor llJ ~ 12. Manufacturer {Later)

Z-u e

ggg E

e P. Liquid Backwash Filter 0

C S l. Quantity 1 a

0. a 0 X 2 Type Mott PHP filter, Cat. No.

~

cL e

{Later) e t) 3o Design pressure 150 a

4~ Design temperature 200 0 5~ Capacity (Later) a~e 6. Housing diameter (Later) 0 70 Porous length (Later)

8. Material CS Ia a 9. Filter grade (Later) Micron

'0 S a Oe Q. PHP Filter Pump a '0 1. Quantity 1 S 0 2~ Type Horizontal, centrifugal a

Em0 30 Total capacity/TDH/NPSH~ gpm/ft/ft 0'

design (Later)

O shutoff (Later)

-runout {Later)

NUMBER

]

SYSTEM DESCRIPTION

~gt CONDENSATE POLISHING SHEET OF Pl CV DEMINERALIZER SYSTEM DATE ~

Al Q

TPO ill

0 Cl

~0 a Q. Cont.

c 0 ~

C) c> NPSH available (Later )

a 5. Fluid Condensate D

6. Design pressure (Later) psig lO r 70 'Design temperature (Later) F

8. BHP at design (Later) oC 9. Material E- {Later)

10. Design standard Hydraulic Institute

~ e 11. Pump motor

~l characteristics (Later) aac o g

~

classification (Later) g 12. Total Weight (Later) lbs

~ 0EJ 13. Location Ot R ea Outdoor O 14. Manufacturer (Later)

D a

ca R. Pressure Dewatering Filter za c l.

g Quantity 1

2. Type (Later)

D 30 Model (Later)

~ aCl 4 Filter area Vl (Later)

~I

~l D

5. Dimension, L x W x H (Later)

6. Capacity (Later)

R a c

I ey Si Diaphragm Pump Ill ~

e 1~ Quantity 1 cJ E

2. Type Horizontal, centrif ugal QJ 3. Total capacity (Later) o

~o 0

TDH (Later)

I: 5. NPSH (Later) acia aecJ 6. Fluid Resin slurry a 7. Design pressure (Later) a o 8 Design temperature (Later)

~e 4P VI 9. MateriaL (Later) 0 g 10. Pump driver Compressed Air llew Total weight {Later) 0 ~ 12 Location Outdoor

'3.

Manufacturer (Later) e"0

~o 4 0 UNRESOLVED MATTERS C

a 0 4.1 Deleted

'0 'D a

~l v0 4.2 Paxameters in Section 3 ~ 3 for the equipment/component will EmO be available from Seller, CJ w 'D 4,3 Spent Resin Handling subsystem.

4.4 & 4.5 Deleted NUMBER SYSTEM DESCRIPT ION 5177-088-M-1 CONDENSATE POLISHING SHEET OF 16 17 DEMINERALIZER SYSTEM DATE TPO

S7 0 0 g 0 ~

5 0 REFERENCES a

a 0 5. 1 Drawings a A Process and Instrument Diagrams sv ra 1. P &ID 5177-088-M-3,. Condensate Ev Polishing Demineralizer v System aOl a 2 P&ID 5177&88-M-5~ Condensate Q

ax Polishing Demineralizer

~

a 0Q Spent Resin Handling System 0 cv R

3. P &ID 5610-M-2~, Condensate and 0 ~ Peedwater System C

C a 4~ P&ID 5177-090-M-3, Demineralized 0

Water Storage and Deaeration System

'I E

~CL 5~ P&ID 5177-086-M-3~ Secondary System W Wet Lay-up System a g a

E a 6. 5610-M-21, Heat Balance a

a a 100% of -Rated Plow a

I B~ System Flow Diagram Ill ~

I a E

5177-088-M-2~ Condensate Polishing Demineralizer UJ

!n a System e

0 S

C aa' Q 5 ' Specification a uX aa

~

l. 5177-088-M-112, Condensate Polishing Demineralizer Ca Qa a g 2. Deleted N

a 0v O 5.3 Turkey Point Units 3 & 4 Plant Design and Mechanical Design Criteria, 5177-M>>OOO I, a

'Da a C

5.4 PC/M 78-81B/82B Condensate Polishing Demineralizer System g0 a

~

C 0 a

Ema Q

~0 'D0 CL R ill NUMBER 5177-088-M-1 Cb SYSTEM DESCRIPTION C SHEET OF CONDENSATE POLISHING 17 8 gpc~~'PO DEMINERALIZER SYSTEM DATE.

COAL'NG RULES il'ilillllllllilllllilllllillllllliliilllllllllilll

'1st 2 1 ~ 1 ~ fat>> 0 4 s e 10 H ts ia 70 n 7 74 7~ a 7 ~

2 IIII 0

I I

I 1

i 3

i

~

I

~

I

~

I 1

I

~

I

~

I 0 ff I I I 0I I I

~ >>

I I 71 I

~

I

~ 10 I I I 0 2*

!!"(TPI I I I i I I I)I I I I I I I 2!

1 "Pif/Pi 4 I ~ ~ ~ 7 ~ ~ fl 3 !<<I<<i<<i<<i 4 7 I

1 I

I I I 1

t 5177-088- M -2 l,

2 I

180M CONDEHEATE PULIF OIKCHAROC 3 SGIO-M.Z/78 Sl( ) I I

C4 Io Ha. I YCEDhM73R HTN t4

'5610- M t /78 81 ( ) 5 ILC Ta 82CKWAEH 25 5111 DSS M.C (G 6)

RECEIVER TANK t FROM DEMINCRALICED 15 24 25 WATER EIOIMILC YANK IO 5177.090-M-Z ( ) 14 )

~F850 7

7 OECICN 1LOW 37560M CONDENSATK BACKWASH POMP 004ICN TDH ~ hd 07

! FILItR F ILIER HLIER FILIER DEMI<<ERALIK ER OEMINERALI'CEN DCMINERALI'EER DEIHINERALIKCR VC SEC L A VES'LEL B VESSEL 6 VtSKKL D taw EXCHANGE 3T66A ~mr.aa ~316 2 C ~3166D ARCA ~ leaa FT 3 3 IO Pss 8 (178 00 0) f; 8'3 12

~

27 DEII4N FLOW' 5 GPUI 17 DECI6N ID<< id (n0000'IFI Q

~ )7

~3086S ~SPSCC; 0 0'

12

~3086O z (j 9 8 9 8 8' 8' 8

3

) HOLDING PUHP ) hOLDING PUMP 18

) HOLDING PUMP 18

) HOLDING PUMP I>> To BACKW05H 20 5171-OSS-M-4 (H-/')

RECEIVER TANK

~37 CI I ' PAECCA'T TANK NOM. CA 04CITY*Nd GALLONS 31 32

) ~3P$ 1A NOTES:

OECIOM Flaw 114001N I. THE CATA SHOWN ON 1<<le FLOW Dl*GIEAM ARE FOR DECIGH DECIGH ION* M 01 PRECOAT PUMP PURPOSES ONLY, AND WHILE O0EOVL AS GVIDFS IN OPERATION, DOES NOT IIEPRECKNT EXACT Olt GUARANTEED OPEAATING CONDITIONS.

LEGEND: THE NVNCEltt 50tH<< EECE AEC HAXIMOH VALOCC OCVCRING OVRINC TEI5 MODE OF OPERATIOH.TXE GRAVER INCTRVCTION I'JHVAL SHOULD 55 CONSVLTED FOR A FROM 0ERVKE PRIMARY PIPING BETTER VHDCR3IAHD<<IO 00 SYSTEM OPERATION A/R 51C SCCONCAR'E PIPING 22 )- DVCI'RECOAT EI t 23 3 TANK RECYCLE ONLY

~3163 A<<l OUafttE RE'3EAVOIR Naht CAPACITY'00 FT HOIE 3)

MODES (NOTE 2)

PARAMETER Qi QE 3 QC 5 e 07 Qe Qs 0)o Q) 0)3 0)000 Qe QB GD02) QGG4025 GIGS 029 OD 03i 032 0>>034 GBGGS038 0>>04D Oi g4 043 Q44 Q45 00080$ $ 052 0- 05 (+55 Qse FILTRATION/ FLOW IGPM) IN!Id f3080 4ati 40ZI 1388 0 fae 105 DEM)NERAL)ZAT)DN TEMPERATURE ( F)

AIYD HOLDING

/067 1061 f081 fae f08'7 f0&7 foe'7 /20 110 Tf PRESSURE (PS(G) 392 300 MO 311 32II 323 2i BY-PA35 FLOW (GPM) l3107 1$ 010 fiwlt /H10 f3110 ~4 fl,e 05 lai 105 APEF DPERAT)DN TEMPERATURE ('F) feet fea.l fall.i 031 017 fte Ite f 20 /2O

(>>LL 1/0 Yt'iitMaff seas PREGCURE (PS)G)

FLOW (GPM) 391

>>HO 312 Mle atl tati

\'lZ UHO 392 0

0 Zf 20 I'75 313 315 375 375 M SM SCM

'ARD BAC)(WASH)NG TEMPERATURE i F) reel 04 7 0~ I Cll 1 fdi '117 cll I Iea ea fde fte fto 20 fta fZO l20 I zo PRESSURE (PeiG) 380 140 3Z0 ite 392 41 ~I N 10.00 IOO 30- 4s Of->>0 FLD)V <GPM) Ms 4at7 4atl l3Ms 0 l940 Nfd aal 0./940 740 lese I'14 0 GENERAL IJPDATE PRECDAT)NG TEMPERATURE ( F) feel 11 Ssl 1st 07 Sil 108.7 00 100 Iza fco 00 Iee fie ISSUED FCR USE PB /7 PRESSURE (Pe)G) 380 Sle He iti 392 328 20 5 5 2 0

FLOW (GPM)

TEMFERATURE (eF) BECHTEL PRESSURE (Ps)G) OAITHENCCURO. MARYEA 0 LDW (GPM)

EMPERATURE(sF)

REGSURE (PSIG I ELDIIII IDIEI I LIIIE CONEIIE TURKEY POINT NUCLEAR UNITS LGW ( GPM UNIT Ma. 3 atf<<>>00 Mw Net>>LLh 0>>

('F ) Uf 7 Uo. 4 07~40 W f at>>sf>>7>>M

'RESSURE EMPERATURE (PeiG'I SYSTEM FLOW DIAGRAIYI FLOW (GPU) jt TE M PE P AT U RE RESSUAE

('F )

(I eiG)

CONDENSATE POLISHING DEMIINERALIZER SYSTEM DESIGN TEMpERATURE (eF ) zao zao zoo zoo zoo zao zaa zaa zao zoo zao zao zoo zao zoa zaa zoa tao zao zaa Ha fto IKD lzo zoa zaa oo zoo fto I'ZO l'Za fza ta I za sT CONDITIONS PRcSSURE (PeiG) 545 545 545 545 545 545 545 545 545 545 545 545 545 45 54>> 545 545 545 545 545 545 oa faa ao tao ao fao lao fao fag 5I77-088- M -2 r'~~"j- PC/M 78.8)B/82B FILE NUMBER:

1 8 )ID42 I

~

c~~

d tl f1 ttul ~~

tlf~ t tlf s it I~ ite el if1 cs t~ I 7\.

ed t ~ 71 f ~ ~ ~

tf ~ dst st ~ t d lihel idt Ie th\ 0 ~ I

~ d that tt 11 s c ~ te te sd etta 7 1st dsc tis) 7 1 ttcd,tp yc si ~ hhlct.

02 EAAO3R07132722~CK029480 309227130~~