NIT NO.: PNMM/PC161/E/001 CORRIGENDUM -4.0 …pdilin.com/pdf/Corrigendum-IV-Technical-452018.pdf ·...

S. No

1.

2.

3.

4.

5.

6.

Part / Sec

Part II : TechnicSection - 4.0,

Part II : TechnicSection - 2.0, Part II : Section & Part II : Section - 4.0,

Part II : Section - 4.0, Part II : Section & Part II : Section - 5.1 , Part II : TechnicSection - 3.0, & Part II : TechnicSection - 9.0

COR

P

cal 3

cal 3

Technical - 3.0,

Technical

5 & 1

Technical 2

Technical - 4.0,

Technical

5 & 6

cal

cal

13 & 3

WTP ,D

RRIGENDUM

Page Cla

3 of 28 2.1

3 of 6 2.0

5 of 34

&

17 of 28

1.1. & 3.2

20 of 28 3.3

5 of 28

&

6 of 8

3.1,& 5.0

13 of 34, 32 of 34

&

3 of 32

1.1.Sco 6.0 TwoRecSpa & 2.0 PAR

DM & CPU PNIT NO.: P

M -4.0 TECHN

ause No. D

L

T3#

.1

(14)

OtwwaC&CcotoinW

- 7 (b) Mh

, 1

W R&F

.4.2 Static ope,

Spareso Years commended ares

SPARE RTS FOR

Spaatp

Tspid&2

PLANT; HURPNMM/PC16NICAL( PRO

Description

amella clarifier

Treated Water Qua#

One (1) no. neutrawo compartmentwith integral pipe

ccessories commCPU regenerati& Capacity: Capaciompartment shallo hold waste waten 24 HWPTP+DM+CPUMixed Bed : Cycle

ours Water Pre Treatme

Retention Time &

lash mixer : 5 MinSupply of manda

arts for two yeand commissionttached elsewheackage,

Two years normapares required

dentified by t&

.1 to 2.11

RL GORAKHP61/E/001 OCESS), DAT

AM

ality : SDI <

alizing Pit in ts complete e, valves &

mon for DM & on waste.

ty of each l besufficient er generated

Hrs. For

time :68

ent Plant:

: 1 Mins

ns atory (spare r operation) ing spares ere in bid

al operation are to be

he bidder.

PUR

TE:04.05.201

MENDMENT TYPE M/D/A/C

A Lamequ Bid

A SD

C Regshaacc

M Cyc

C Venthe Howflas

C WeSecMabidd BidRecto tparour

18

A

mella Clarifier /uivalent to be cons

der to submit PTRI at WPT outlet no

generated effluenall be transferrecordingly Neutralis

cle time shall be 7

ndor to provide air design

wever, Minimum sh mixer shall be 1e understand thction-9 (clause 2ndatory Spares ader within the Lum

der needs to scommended Sparthe Mandatory Sprt of quoted Lumr understanding.

Amendment

/ HRSCC/ Tubsidered.

R of the same aloot to be considere

t only from DM aned to Neutralisasation Pit shall be

72 hours

adequate retentio

Hydraulic Reten1 min. hat spare Parts 2.1 to 2.11) arend the same shal

mp SumPrice.

submit the Sepres (2 Years Sparpares" and same

mp Sum Price". P

be Settler or

ng with Bid. ed

nd CPU Plants ation Pit and

designed.

n time as per

ntion Time for

as listed in e referred as l be quoted by

arate List of res) in addition e shall not be Please confirm

7.

8.

9.

10.

11.

12.

Part II : Section - 2.0

Part II : TechnicSection - 2.0, Part II : Section - 2.0 Part II : Section - 4.0

Part II : Section & Part II : Section - 4.0 Part II : TechnicSection - 2.0 & Part II : TechnicSection - 4.0

COR

Technical 2

cal 3

Technical 4

Technical 3

Technical - 2.0

Technical

2 & 5

cal

cal

4 & 5

WTP ,D

RRIGENDUM

TWOP(MASPA

2 of 6 1.1

3 of 6 1.2

4 of 6 2.0

3 of 28 2.1

2 of 6

&

5 of 28

1.1 &3.1

4 of 6

&

5 of 28

2.0 &3.1


M -4.0 TECHN

WO YEARS ERATION ANDATORY ARES ): R

T

TIr

TC

Tfeb

RT&WIn

TT&W(1GT


Raw Water

Temperature : Amb

Turbine Condensron as Fe : 0.2 Treated WaterColloidal Silica as SThe raw water shaed to flash mixere mixed with Alum

Raw Water: Turbidity : & Water Pre Treatmenlet Turbidity : 100

Treated Water QuaTurbidity : <1 NTU& Water Pre Treatme11) Dual Media Fi

Guaranteed EffluenTurbidity : <2 NTU


bient

ate Quality:

r Quality: SiO2 : BDL all be directly rwhere it will m/FeCl3,

50 NTU

ent Plant: 0 NTU

ality:

ent Plant - lters nt

PUR

TE:04.05.201

M Fol UtiliMin/ RawDM ProcProcTurbSteaTurb

C Iron

C Remreq

C Alu

C Des

C Tur

18

lowing shall be op

ty Facilities: Tempe/Nor/Max/design)

w Water : -/AmbienWater: -/25/-/70

cess Condensate (Acess Condensate (Ubine Condensate ( Aam/Turbine Condebine Condensate ( On mentioned as Fe

moval of Colloidaluired. m/FeCl3 can be u

sign turbidity shal

rbidity Guarantee

perating / design p

erature (Deg C)

nt/47/-

Ammonia Plant): - /Urea Plant): - / 50 /Ammonia Plant): 40nsate (Urea Plant) O&U): - / 50 / - / 80e is 0.2 mg/l.

l Silica in WTP pla

used as floculant

l be 100NTU

values shall be <2

parameters:

/ 47 / - / 85 / 70 / 120 0/ 46.1 / 50 / 70 : - / 50 / - / 85

0

ant is not

2 NTU

13.

14.

15.

16.

17.

18.

19.

20.

Part II : TechnicSection - 4.0 & PID No : PC161

Part II : TechnicSection - 4.0 & PID No : PC161

Process FlowWater Pre TreDwg No 7112/7/7113-00& Part II : Section - 4.0 Process FlowCondensate Po

Piping and InstrDiagram DM Water PlantDwg No : PC16Piping and InstrDiagram DM Water PlantDwg No : PC16Part II : TechnicSection - 4.0

Part II : Section & Part II : Section - 4.0

COR

cal

1-7316-0027

2

cal

1-7316-0027

2

w Diagram eatment Plant

: PC161-046

Technical

7

w Diagram olishing Unit

rumentation

t 61-7113-0024

rumentation

t 61-7113-0024

cal 1

Technical - 4.0

Technical

1

WTP ,D

RRIGENDUM

21 of 28 3.4

21 of 28 3.4

7 of 28

ProDiaPrePla (11Filte

12 of 28 3.2 (2)Filtr

12 of 28 3.2 (2)Filtr&4. UPum


M -4.0 TECHN

TCT&CT

TA(2&A(3

ocess Flow gram (Water

e Treatment nt)

) Dual Media ers

N6&N(7

C

CL

S

DM Plant: Ultra ration

NP

DM Plant: Ultra ration

UF Feed mps

F&NC


Turbine CondensaCartridge Filter FeTwo (2) & Cartridge Filter FeThree (3) nos. Turbine CondensaActivated Carbon F2)

& Activated Carbon F3) nos.

Number of Dual Me+2,

& No. of Dual Media 7W+1S)

Condensate Off-Sp

Chemical Dosing aine

SMBS and Antisca

No. of Skids : Two(Permeate Flowrate

eed Flowrate : 18& Numbers : Three (2Capacity : 120 m3/


ate Unit: (2) eed Pumps :

eed pumps :

te Unit: (3) Filters: Two

Filter :Three

edia Filters :

Filters: 8

pec to ETP

at SAC outlet

alant Dosing

(2) e : 160 m3/hr

80m3/hr

2W+1S) /hr

PUR

TE:04.05.201

C Car

C Act

C No.

C ConCliebatt

C No befo

M SM

A UF per

C Totwor

18

rtridge Filter Feed

ivated Carbon Filt

. of Dual Media Fi

ndensate Off Speent pipeline. Biddtery limit.

chemical dosingore degasser

BS dosing is not

Skid shall be 2Wrmeate flow shall b

al UF Feed florking will be 240 m

d Pumps shall be T

ters shall be Thre

lters shall be 8 (

ec shall be routeder will make al

g is required af

required at UF ou

+1S and each stbe 120 m3/hr.

ow with Two(2) m3/hr

Three

ee

(7W+1S)

ed to ETP By l provision till

fter SAC and

utlet

tream

nos. pumps

21.

22.

23.

24.

25.

26.

27.

28.

29.

30.

31.

32.

33.

Part II : TechnicSection - 4.0 Part II : TechnicSection - 2.0,




Part II : TechnicSection - 3.0


Part II : TechnicSection - 4.0 Part II : TechnicSection - 4.0 Part II : TechnicSection - 4.0

Part II : TechnicSection - 4.0 Part II : TechnicSection - 4.0 Part II : TechnicSection - 4.0

COR

cal 1

cal 3

cal 6

cal 6

cal 5

cal 5&6

cal 3

cal 6

cal 7

cal 9o

cal 1

cal 1

cal 1

WTP ,D

RRIGENDUM

12 of 28 2.a)

3 of 6, 1.3

6 of 6 3.1.

6 of 6 2.3.

5 of 34 iv &

5 of 34 & 6 of 34

1.1.& x) a

3 of 28 B

6 of 28 6

7 of 28 9

9 of 28&6 of 8

16&

12 of 28 2

19 of 28 7.a

19 of 28 7.b


M -4.0 TECHN

) M

P

.7 La

.6 T

& v A

.1.n)

and g)

A

DP

C

S

&5.0 Cta

U

C

Tca


MWCO for UF

Process condensa

ist of laboratory innd equipments

Total Silica at MB o

ACF backwash pu

Auto valves

Design Capacity– Plant

Chemical house

Sludge sump

Capacity of Fire waank

UF skid capacity

Capacity of SAC ex

Turbine condensatapacity


te quality

nstruments

outlet

mps

DM Water

ater storage

xchanger

te plant MB

PUR

TE:04.05.201

M MW

M In PAmPlacon

M apalabofor

M VenoutPla

C ACconby F

C All opefor

C 240

A 30 stor

C slud

C cap410

C Outeac

C BidDM

C Mixconeac

18

WCO for UF shall b

Process condensamonia B/L and thnt should be d

ntaminant and quaart from lab inoratory ,bidder shday to day operat

ndor to guaranteelet of MB in Cont. F backwash pum

nsidered if not reqFeed Pumps by Bauto valves abov

erated butterfly vadrain valves on ve

0 m3/hr net output

daysto be consrage area in chemdge sump is Singl

pacity of Fire Wa00 m3

tput capacity at Uch stream der to fix capacity

M / CPU Plant xed bed is comndensate and turch mixed bed shal

be 10 KD

ate quality, two vahe other for Urea designed on higality as per Flow sstruments providhall provide all lation of WPT/DM p

e Total Silica (asndensate Polishi

mps and blowersquired and the samBidder. ve 150 NB to be alves (Leakage clessels.

t is required at UF

idered for designmical house. le compartment

ater Storage Tank

UF plant shall be

y as per the Plan

mmon for both rbine condensatell be for 300 m3/h

alues - one for B/L However,

gher value of scheme. ded in main

ab instruments plants.

s SiO2) at the ng Plant/ DM

s may not be me is replaced

pneumatically lass V) except

F outlet.

n of chemical

kshall be 2 x

120 M3/hr of

nt capacities of

the process e. Capacity of r

34.

35.

36.

37.

38.

39.

40.





Dwg. No. PC16Rev. 0


General

COR

cal 1&2

cal 2

cal 2

cal 2

61-7318-0028 1

cal 5

WTP ,D

RRIGENDUM

18 of 28 & 22 of 28

3.3 & 3.4

21 of 28 3.4

25 of 28 5.1

25 of 28 5.2

1 of 1

5 of 6 2.1


M -4.0 TECHN

- 3.a

- 3.a

G

(2, 3) Tnpfil

M123b4pM 12d3st4psoP

Td

D(G


Grade of Activated

Turbine condenso. of cartridge filteump and activatelters

MOC of tanks ) Anion Hot water) Acid dilution tan) Acid dilution taned) ) Acid tank for neuit

MOC of piping

) Acidic water ) Alkali (sodium hilute ) Alkali (Sodium htrong ) Waste effluent frlant vessel & chemolution tank

Piping MOC

Treated water qualrinking water plan

DM Plant - ChemicGuarantees)


d carbon

ate unit - er feed d carbon

r tank k (Cation) k (Mixed

utralization

ydroxide)

hydroxide)

rom DM mical

lity at nt outlet

cal dosages

PUR

TE:04.05.201

M ActPro

C cartfiltecomcon

M MO

M MO

A Pipfrom

C In cGuaload

C RegalonBidPMdosBidin th

18

ivated carbon socess and turbine

tridge filter feeders shall be threemmon for both prndensate.

OC of MSRL/ CS F

OC of MSRL/ CS F

ing MOC upto SAm SAC shall beMS

case of variation inarantee Deviationd variation.

generation reactng with resin curvalong with minimC/Owner reserv

sage. der has to mandheir technical bid

hall be of deoilcondensate.

pump and acte (2W+1S).Three rocess condensat

FRP lined to be co

FRP lined to be co

AC shall be SS 30SRL.

n Raw Water quan will apply on ove

tion stoichiometve to be submitte

mum chemical conves the right to

datory submit the

ing grade for

ivated carbon MB units are

te and turbine

onsidered.

onsidered.

4 and further

lity, erall chemical

ric equations d in Technical sumption/m3

o assess the

above details

41.

42.

43.

44.

45.

46.

47.

48.

49.

50.

51.

52.

53.

General


Part II : Technic4.0 & PFD

Part II : Technic4.0 Process Flow D

General

Part II : Technic4.0 Part II : Technic2.0

Part II : Technic2.0 Part II : Technic2.0 Part II : TechnicSection - 3.0



COR

cal 5

cal, Section- 7&P73

cal, Section- 1

Diagram P73

cal, Section- 4

cal, Section- 3

cal, Section- 3

cal, Section- 6

cal 1

cal 2

cal 5

WTP ,D

RRIGENDUM

57/1510

7 of 28 & PC161-7112/7/7113-0046

3.1

12 of 28

PC161-7112/7/7113-0045

4 of 6

3 of 6

3 of 6

6 of 6

16 of 34

27 of 34

5 of 6 3.1.


M -4.0 TECHN

C

Sch

(11) N

3.2 (2) NS

Au

F

2.0 T

1.2 TA

1.3 PA

2.3 Tco

1.1.6.1 GseCn

4.0 M

.6 Sp


ClO2 system

tilling chamber / Ihamber

Number of working

Number and Capackid

Air Blower for DMFnits

ire Fighting Syste

reated water qual

urbinecondensateAmmonia, Urea an

Process CondensaAmmonia and Urea

otal silica in Polisondensate

General scope ofervices–

Construction/Erecto:1.28 Hazop stud

Mechanical mainte

Scope w.r.t Inteiping between


nlet

g DMF

city of UF

F and MB

em

lity

e quality nd O&U

ate quality a hed

f Work and

tion clause dy

enance

erconnecting O&U and

PUR

TE:04.05.201

C ClOchlochlo

A Stillchloacc

C Duanos

C UF per

A BidDM

C Fireent

C 1. pcor

C Silicconcon

C MeO

M Guain P

C Extbe c

C Hydcon Quabidd

C Ple002

18

O2 dosing Systeorination. Capaciorination shall be ling chamber orination of raw wceptable. al media filters shs.(7working+1Stan

Skid shall be rmeate flow shall bder to consider se

MF and MB units

e fighting systemire plant is in clienpH value of 6.5-8rrection (if requireca as SiO2 <0.ndensate qualitynsidered as ReactOH max 20 ppm i

arantee of Total sPolished condensaernal agency / Econsidered by Bid

dra, Fork lifts, Crantractor scope.

antity shall be asder ase refer the

23/24/25/26/27/28

em shall be for ity of ClO2 genemin 5 kg. or inlet chambwater before the

hall be 8 ndby)

2W+1S and be 120 m3/hr. eparate air blower

m & Fire protectiont’s scope of supp8.5 shall be maintd) by bidder. .02 ppm as inley Ammonia plative Silica. in inlet of CPU

silica shall be SiOate.

Examiner for Hazodder.

anes etc will be in

s per requirement

P&ID no PC168/29

pre & post erator for pre

ber for pre-flash mixer is

each stream

rs(1W+1S) for

on system for ply. tained, with pH

et for Turbine ant shall be

O2 < 0.01 ppm

op study is to

n the supply of

t of successful

61-7112/7113-

54.

55.

56.

57.

58. 59.

60.

61.

Part-II TechnicaPC161-G-101-P

Process flow diaPC161-7112/71



General Part II : TechnicSection - 2.0,



COR

al P-II/1.0

5

agram 13-046

1

cal 2

cal 6

cal

cal

cal

WTP ,D

RRIGENDUM

5 of 6 3.1.

1 of 1

28 of 28 7.0

6 of 20 5.6

2 of 6

2 of 6

3 of 6


M -4.0 TECHN

fa

.7 Cla

Pwfirco

Cplimdvab

It CpsuinfoO

1.1 R

1.1 RwBT

1.2 TC


acilities under Bidd

Chemical lababoratory requirem

Process flow diagrw.r.t fire water tankre water pumponnecting pipes.

Cooling water rovided at the Imit by clienistributionof plaarious distributione done by Contrashall be the res

Construction corovide uitableaccommod

ncluding necessaor their labour andO & M power costRaw water Quality

Raw water Qualitywater quality avaiBattery Limit of Treatment plant (W

Turbine CondensaConductivity


der’s scope

-Minimum ment

ram - Scope k & Nozzles, ps & inter

shall be SBL battery

nt. Further ant air to n points shall ctor. ponsibility of ntractor to

dation ary facilities d staff.

y - Feed raw ilable in the

Water Pre WTP)

te Quality –

PUR

TE:04.05.201

C Apalaboday

C fire in thP&I002

C Ple

C LanLanandis b

C AppM Bid

ana

Rev

M TherawPLAactuper

C Conto b

18

art from lab inoratory,bidder shy to day operation

water pumps &he scope of ClienID. Please refer th23

ase refer the P&I

nd for labour colond For temporaryd area for offices)basis

proximate 10 Rs/ der to consider th

alysis report enclo

vised Raw water quality.pdf

e DM plant shall w water analysisANT capacity outpual input water qrformance test. nductivity in the tuboiler feed water d

nstruments providall provide lab in of WPT/DM planinter connecting

nt which is alreadyhe P&ID no PC16

ID no PC161-711

ny shall be arrangy facility (store fa) shall be provide

kwh he latest / revised osed.

be designed bass given in NIT put shall be assesquality available a

urbine condensatedosing chemicals.

ded in main nstruments for ts. pipes shall be y shown in the 61-7112/7113-

2/7113-0023

ged by bidder. abrication yard d as is where

raw water

sed on design however DM

ssed based on at the time of

e shall be due

62.

63.

64.

65.

66.

67.

68.

69.

70.

71.

Part II : TechnicSection - 2.0, Part II : TechnicSection - 2.0,

Part II : TechnicSection - 2.0, Part II : TechnicSection - 4.0


Part II : TechnicSection - 3.0, Part II : TechnicSection - 4.0, Process Flow DPC161-7112/7/7Part II : TechnicSection - 3.0,


COR

cal

cal

cal

cal

cal

cal

cal

Diagram 7113-0046

cal 2

cal 2

WTP ,D

RRIGENDUM

3 of 6

5 of 6

5 of 6

7 of 28

21 of 34

4 of 34

12 of 28

21 of 34 4.0

22 of 34 4.0


M -4.0 TECHN

1.3 P

2.2 PD

2.3 PC

1.0 T

1.1.1 TPC

1.1.1 FC

2 U

VT

It opmin CdinopreuM

T/fofch


Process Condens

Polished water QuDM Plant

Polished water QCPU

Turbine condensat

Turbine CondensaPlant : QuantityCarbon filter.

ire water stoCapacity UF Capacity

Vendor scope – FirTank & filter water

may also be meperation of WPTlants during the

months is expecntermittent.

Contractor to planeployment

ntermittent peration of WPTlant during first equirement of Area plant contract

Mechanical Maint

Top up/ replacemefilters media, & ref vessels, acid/alhemicals shall als


ate Quality

ality From

Quality From

te Quantity

ate Polishing of activated

rage Tank

re water tank

entioned that TP and DM e initial 12 cted to be

n manpower considering

TP and DM year as per

Ammoniaand tor. tenance

ent of resin’s epair of lining lkali & other so be in the

PUR

TE:04.05.201

C In pcon

M Silic0.0

M Siliccon

C turb300

C Act

C Firecum

C UF per

C Firesco

A Thereqthe

R

A Supfor durtriaPre3 m

18

process condensnsidered. ca in DM water s1 PPM

ca in Polishednsidered as less th

bine condensate 0 m3/hour

ivated Carbon Filt

e water storage tm Skid shall be 2W

rmeate flow shall be water Tank & filtope e month wise Puirement scheduir manpower depl

UTILITIES REQUIRED.pdf

pply of all chemicthe Operation a

ring start-up, pre-cl runs and perform

eliminary Acceptanmonths during O&

ate no silica and

hall be considere

d waterfrom Chan0.01 ppm.

shall be (1W+1S

ters shall be Thre

ank capacity sha

+1S and each stbe 120 m3/hr. ter water tank sha

Process water le is enclosed. Boyment according

cals and consumaand Maintenancecommissioning, comance guarantee nce Test of comp

&M period shall be

d iron is to be

d as less than

CPUshall be

S) of capacity

ee

all be 2X 4100

tream

all be in bidder

& DM water Bidder to plan gly.

ables required e of the plant ommissioning, test runs upto

plete system + e in the scope

72.

73.

74.

75.

76.

77.

General


Part II : Technic4.0,

General

General

General

COR

cal 3

cal, Section - 4

WTP ,D

RRIGENDUM

3 of 6 1.2

4 of 28 2.2


M -4.0 TECHN

sc

T

& 1.3 C

G

C

WC

B


cope of contracto

Termination points

Condensate influen

General - Turndow

CLO2 SYSTEM

WPTP -Consumption (Gua

B.L Pressure of ut


r.

s

nt quality

wn

Chemical arantees)

ilities

PUR

TE:04.05.201

of sandrefe It iscomin bDMcomher

M Tie Conown Bidsha

C Oil

M Minbidd

C CLOForDos

BidconPMdos Bidin th

M Folpre0.5 1) C2)S3) P

18

supply of the Vend Treated water erred for considera

s further clarified tmmissioning of 1 sbidders scope. Th

M water reqmmissioning of onrewith.

in points/Coorndensate Polishiner at package ba

der to provide tall be finalised durcontent to be con

nimum Turndown der’s scope shall

O2 System: For Rr Drinking water 1 sing Pump: (1W+der to sub

nsumption/m3 figC/Owner reserv

sages.

der has to mandheir technical bid lowing utilities ssure indicated bkg/cm2):

Cooling water makService water PumPolished/DM wate

dor. The month wrequirement scheation of chemical

that chemical constream till PAC ofhe month wise proquirement schne stream to PA

rdinates for WTng Plantshall be

attery limit.

their layout.Furthring detailed enginnsidered as free o

ratio for the Plantbe 50 %

Raw water 5 kg/hr kg/hr (1W+1S)

1S) for each bmit minimumgures in their tves the right to

datory submit the shall be made elow at Vendor’s

ke up pump : 6.5mp 6.0 kg/cm2g er transfer pump 6

wise DM water edule may be consumption.

sumption after f plant shall be ocess water & edule from C is enclosed

TP, DM and e provided by

her, the same neering il.

t under

(1W+1S)

m chemical technical bid.

o assess the

above details

available at battery limit (±

kg/cm2g

6.5 kg/cm2g

78.

79.

General


COR

cal

WTP ,D

RRIGENDUM

5


M -4.0 TECHN

1.4 SG


Sustained LoaGuarantee


ad Test

PUR

TE:04.05.201

4) Kg/5) 7.0 Howfiguof mut

C ForonlyFolconA) 1) F2) F3) D4) F5) L6)C B) D1)D2)D3) U4)R C) C Pro1) A Tur1) C

M Durdemmin95%

18

Drinking water p/cm2g. Drinking water pKg/cm2g.

wever, availabilityures at battery limany variation betually agreed. r calculation of gy continuous runnlowing continuou

nsidered WTP

Flash mixer &FlocFilter feed pump DM Plant feed pumFeCL3 Dosing pumLime Solution DosCLO2 Dilution pum

DM Plant Degasser water traDegasser Blower UF Feed pump Regeneration Wate

CPU ocess CondensateACF Feed pump

rbine CondensateCartridge filter feering the Sustainemonstrate that thenimum of 7 days % of the rated cap

pump for plant di

ump for Townsh

y of above utilitiesmit shall be finalizeeyond the, the s

uaranteed powerning motor shall beus running driv

culator

mp mp sing Pump mp

ansfer pump

er pump

e :

: ed pump d Load Test the

e WPT,DM & CPUat an aggregate

pacity.

istribution: 7.0

ip distribution:

s with pressure ed and in case ame shall be

r consumption e considered. ves shall be

contractor will U operate for a output of min.

80.

81.

LEGEND

M: MOD

General


D:

DIFICATION, A

COR

cal

A: ADDITION, D

WTP ,D

RRIGENDUM

5 of 6

D: DELETION,


M -4.0 TECHN

2.2 PD

C: CLARIFICA


Polished Water QDM Plant / CPU (G

ATION


Quality From Guarantee)

PUR

TE:04.05.201

C ForshaTurnorcon

M Tot

18

r Stream #1 of Wall mean the opern down capacity rms on manual ntrol system) al Iron content as

WTP & DMW, Ceration of Streamand as per guamode (excluding

s Fe shall be <0.0

Commissioning m or Plant at arantee quality g PLC based

01 mg/kg

NTPC Energy Technology Research Alliance (NETRA) GREEN CHEMISTRY LABORATORY

NTPC Energy Technology Research Alliance (NETRA) E-3, Ecotech-II, Udyog Vihar, Greater NOIDA(U.P.)-201306 Page No. 1 of 2

INTER-OFFICE MEMORANDUM

From: To:

Our ref.: Your ref.:

Date: Date:

Kind Attention: Sh.

Dr. R. Das

Copy to: 1. Office copy.

NOTE: Kindly return the duly filled feedback form to us.

NTPC Energy Technology Research Alliance (NETRA) GREEN CHEMISTRY LABORATORY

NTPC Energy Technology Research Alliance (NETRA) E-3, Ecotech-II, Udyog Vihar, Greater NOIDA(U.P.)-201306 Page No. 2 of 2

WATER ANALYSIS REPORT

(A) Brief Description:

(B) Analysis result:

SOURCE: PDIL Expressed as Parameter 1193/1 1193/2 1193/3

Temperature oC 28 28 28pH at 27 deg.C * 7.8 7.7 7.6Turbidity NTU 9 14 8Conductivity at 27 deg.C μs/cm 430 450 385Dissolved Oxygen at 27 oC ppm O2 6.5 5.8 6.2Total Dissolved Solids (TDS) mg/litre 314 318 280Total Suspended Solids (TSS) mg/litre 11 18 10P- alkalinity ppm CaCO3 0 0 0 M- alkalinity ppm CaCO3 156 140 122 Total hardness ppm CaCO3 196 170 160 Calcium hardness ppm CaCO3 100 90 70 Magnesium hardness ppm CaCO3 96 80 90 Sodium ppm Na 16 27 20Potassium ppm K 2 5 4Iron - Total ppm Fe 0.05 0.05 0.05Chloride ppm Cl 18 30 30Sulphate ppm SO4 48 40 35 Nitrate Ppm NO3 0.5 6.0 1.0 Reactive silica ppm SiO2 7 11 9 Colloidal Silica ppm SiO2 5 9 5 Zinc ppm Zn 0.02 0.03 0.02 Manganese Ppm Mn 0.01 0.01 0.01

TEST METHOD : IS-3025; Ion Chromatography & AAS

Dr. R. Das /

GREEN CHEMISTRY LABORATORY

1. Testing was done as per relevant methods mentioned. The results are related only to the item tested and as on received basis. The report shall not be reproduced except in full, without the written approval of NETRA (NTPC).

2. Any anomalies / discrepancies in the test report should be brought to our notice within 05 days from the date of issue of test report as samples (if remain) will be disposed off there -after.

UTILITIES REQUIRED AS PER TABLE SCHEDULE

NOTE: 1) Fire water shall be made available by vendor from end of 14th month.

SR. NO.

UTILITY UNIT M14 M15 M16 M17 M18 M19 M20 M21 M22 M23 M24 M25 M26 M27

1 DM Water

m3/hr 25 30 30 30 30 162 162 200 220 330 330 330 330 330

2 Process Water

m3/hr 25 25 25 25 25 560 560 710 570 570 800 800 800 800

3

Fire

Water

m3/hr

NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1 NOTE‐1

4 Potable

Water

m3/hr 30 30 30 30 30 30 30 30 30 30 30 30 30 30

WTP ,DM & CPU PLANT; HURL GORAKHPUR

NIT NO.: PNMM/PC161/E/001 CORRIGENDUM -4.0 TECHNICAL( ELECTRICAL), DATE:04.05.2018

Page 1 of 2

SL. NO

REFERENCE OF BIDDING DOCUMENT AMENDMENT TYPE AMENDMENT

Part/Sec. Page No. Clause No. Description as per NIT/Amendment M/D/A/C

PC161-G001-P-II/Sec.-5.3 rev. 0 04 of 80 1.3 The minimum scope…. C Air pressurization & ventilation system is not required in

cable cellar/gallery of substation.

PC161-G001-P-II/Sec.-5.3 rev. 0 11 of 80 5.1.e) All outdoor lighting … from outdoor lighting bus M All outdoor lighting … from outdoor lighting bus. Aviation

light shall be provided if required as per ICAO regulation.

PC161-G001-P-II/Sec.-5.3 rev. 0 11 of 80 5.2 DC Power…..220 V DC Distribution Board to

be located in the Sub-Station. C

DC Power…..220 V DC Distribution Board to be located in the Sub-Station. For DC battery backup time refer Cl. No. 9.6 b) of doc. no. PC161-G001-P-II/Sec.-5.3 rev. 0 and for ACUPS power (provided by owner) battery backup time is also for 1hour.

PC161-G001-P-II/Sec.-5.3 rev. 0

14 &15 of 80

7.3,7.4 & 7.5

Protective relays shall be of latest version….. part of protective device. C

Protective relays shall be of latest version….. numerical relay having serial port for monitoring. Energy management is in owner’s scope however numerical relay shall have communication on IEC-61850 protocol in redundant mode and meter shall have communication on MODBUS protocol.

PC161-G001-P-II/Sec.-5.3 rev. 0 17 of 80 7.8 Bare minimum protection for power

distribution… C DC supply supervision relay (80) shall be provided in the Switchgear with provision for annunciation locally at switchboard.

PC161-G001-P-II/Sec.-5.3 rev. 0

21 of 80 9.3.1.d &

9.3.3(ii)

LV Switchboard above 1600 Ampere… complete 415V switch boards shall be IP-54. Low voltage switchboards… protection shall be IP 52.

C For IP protection Cl. No. 9.3.1 (d) shall prevail.

PC161-G001-P-II/Sec.-5.3 rev. 0

21 of 80 9.3.5.b 240V single front, non-draw out type Emergency LSDB for power supply to Emergency lighting fixtures. C

240V single front, non-draw out type Emergency LSDB for power supply to Emergency lighting fixtures. LSDB (N) shall be fed from MLDB (bidder’s scope) & LSDB (E) shall be fed from EMLDB (bidder’s scope).

PC161-G001-P-II/Sec.-5.3 rev. 0

24 of 80 9.3.3.x) Motor rated below 75 KW rating… draw-out type in all the switchboards.

M Motor rated below 75 KW rating… draw-out type in all the switchboards. Power feeders of rating 250 Amp. & below shall be fed from SFU (refer PDS 404) and power feeders rating


NIT NO.: PNMM/PC161/E/001 CORRIGENDUM -4.0 TECHNICAL( ELECTRICAL), DATE:04.05.2018

Page 2 of 2

SL. NO



above 250 AMP to 630 AMP shall be provided with MCCB, ACB power feeder shall be provided above 630 AMP.

LEGEND:

M: MODIFICATION, A: ADDITION, D: DELETION, C: CLARIFICATION


NIT NO.: PNMM/PC161/E/001 CORRIGENDUM -4.0 TECHNICAL( INSTRUMENTATION), DATE:04.05.2018

Page 1 of 3

SL. NO



PC161-E001-P-II/5.4 46 of 75 8.1

Pt.d PLC control system C All the closed loop shall be redundant

PC161-E001-P-II/5.4 61 of 75 12

2 Nos. of Level measurement of two different principle shall be provided for

storage tank level measurementC For each storage 2 Nos. of Level measurement of two

different principles shall be provided.

PC161-E001-P-

II/5.4 3 of 75 1.0 Common PLC system for Water treatment package plant.

C Common PLC has been considered for WTP package and bidder to ensure segregation of individual plant level signals at AI/AO/DI/DO card level so as to ensure the reliability of the system

PC161-E001-P-II/5.4 63 of 75 Annexu

re-1 Instruments Accuracies M Accuracy for the instruments shall be % of reading and

shall be supplied with wet calibration certification.

PC161-E001-P-II/5.4

54 of 75 Instrumentation cable trays C For instrumentation FRP perforated cable trays/cable ducts shall be provided as per NIT.

PC161-G-101-P-II/11.0

Instrument vendor list M Additional vendor list enclosed to be consider by the bidders

LEGEND:




Page 2 of 3

Sl. No.

IINSTRUMENTATION ITEM PDIL BIDDER’S REPLY

1 SILICA ANALYSERS FORBES MARSHALL 2 CHLORINE ANALYSER AWA

B&C ELECTRONICS SRL 3 MOISTURE ANALYSERS SERVOMAX

MICHELL INSTRUMENTS LTD TELEDYNE ANALYTICAL INSTRUMENTS

4 GAS DETECTION SYSTEM MSA DETCON INC DETECTOR ELECTRONICS CORP (KIDDE) NET SAFETY MONITORING INC

5 FIRE ALARM SYSTEM TYCO FIRE SECURITY INDIA PVT LTD EDWARD INTERNATIONAL

6 PC / SERVERS HP 7 FLOW ELEMENT: ORIFICE/ VENTURI/ FLOW NOZZLE STAR MECH CONTROLS INIDA PVT LTD

EUREKA INDUSTRIAL EQUIPMENTS P LTD 8 PITOT TUBE/ ANNUBAR MINCO INDIA

STAR MECH CONTROLS INIDA PVT LTD THERMO FISHER SCIENTIFIC

9 ROTAMETERS KROHNE MARSHALL PVT. LTD. YOKOGAWA TOKYO KEISO CO. LTD. ROTA YOKOGAWA GMBH & CO. KG ASA SPA HEIRICH

10 MASS FLOW METER (CORIOLIS TYPE) DANIEL MEASURMENTS 11 VORTEX METER BOPP & REUTHER MESSTECHNIK GMBH 12 MAGNETIC FLOW METER KROHNE MARSHALL PVT. LTD.

E&H 13 PRESSURE & D/P TRANSMITTERS HONEYWELL AUTOMATION INDIA LIMITED

YOKOGAWA LIMITED 14 ULTRASONIC FLOWMETERS DANIEL MEASURMENT



Page 3 of 3

15 GWR MAGNETROL 16 TANK LEVEL INSTRUMENTS ROSEMOUNT TANK RADAR 17 SPECIAL LEVEL SWITCHES (VIBRATION FORK/RF

ADMITTANCE) MAGNETROL

18 TEMPERATURE ELEMENTS (THERMOCOUPLE, RTD) PYRO ELECTRIC INSTRUMENTS GOA PVT. LTD.

TEMPSENS INSTRUMENTS (I) PVT. LTD. GENERAL INSTRUMENTS CONSORTIUM GOA INSTRUMENTS INDUSTRIES LTD

19 RADIATION PYROMETER LUMA.SENSE 20 ELECTRIC ACTUATOR LIMITORQUE 21 SMART POSITIONER FLOWSERVE

FISHER 22 SS TUBES RATNAMANI

HEAVY METAL AND TUBES 23 TUBE FITTINGS (FOR CONTROL VALVES, ANALYSERS,

SAMPLING SYSTEM) COMFIT HYDRO PNEUMATIC ASTEC FLUID CONTROLS

24 INSTRUMENT VALVE MANIFOLD COMFIT 25 INSTRUMENT MINIATURE VALVES COMFIT

26 INSTRUMENTS COMPENSATION, POWER AND CONTROL CABLE

CORDS CABLES


NIT NO.: PNMM/PC161/E/001 CORRIGENDUM -4.0 TECHNICAL(STATIC), DATE:04.05.2018

Page 1 of 1

SL. NO



1 PC161-G-101-P-II/5.2.1 Rev P, 5 of 44, 1.15

Nitrogen filling : All process equipments shall be supplied with Nitrogen filled. In case of equipment assembled and welded at site, it shall be filled with N2 after testing at site. Dry Nitrogen shall be filled at a pressure of 0.5 Kg/cm2g and equipment shall be fitted with a pressure gauge and valve.

M

All static equipments shall be supplied with Nitrogen filled. In case of static equipment assembled and welded at site, it shall be filled with N2 after testing at site. Dry Nitrogen shall be filled at a pressure of 0.5 Kg/cm2g and equipment shall be fitted with a pressure gauge and valve.

3

PC161-G-101-P-II/5.2.1 Rev P

12 of 44 2.2.16 PWHT requirement: Equipment under Caustic, amine, hydrogen, Lethal & sour (Wet H2s) service shall essentially be PWHT with 100 % radiography. The hardness of the parent weld, weld & HAZ shall be Limited to 200 BHN in such cases

M The clause shall be considered revised as follows: Equipment under Caustic service shall essentially be PWHT with 100 % radiography. The hardness of the parent weld, weld & HAZ shall be Limited to 200 BHN.

4 PC161-G-101-P-II/5.2.1 Rev P

20 of 44 3.6.1 Rubber lining thickness : The type of rubber (i.e. Natural, Butyl, Nitrile, Ebonite, and Hypalon etc.), its minimum Thickness shall be 5 mm & hardness shall be decided as per design code/specification

M The clause shall be considered revised as follows: The type of rubber (i.e. Natural, Butyl, Nitrile, Ebonite, and Hypalon etc.), its minimum Thickness shall be 4.5 mm & hardness shall be decided as per design code/specification.

LEGEND: M: MODIFICATION, A: ADDITION, D: DELETION, C: CLARIFICATION


NIT NO.: PNMM/PC161/E/001 CORRIGENDUM -4.0 TECHNICAL( PIPING), DATE:04.05.2018

Page 1 of 1

SL. NO



1 P-II/ Sec.5.2.3

(Design philosophy-

Piping) PMS/VMS A

Following Pipe classes are attached : a) B24RL for CS rubber lined,

Equivalent BIS specification shall also be acceptable.

b) B24P for CPVC

2 P-II/ Sec.5.2.3

(Design philosophy-

Piping) PMS/VMS A

CS FRP lined piping material specification : Material specification shall be as per pipe class B24RL except rubber lining. Specification for FRP lining shall be as per manufacturer std, which shall be provided at bidding stage.

LEGEND:


Class: B24P

PROJECT NO. PC160/161/EM250PIPING MATERIAL SPECIFICATION

SERVICEETP

TEMPERATURE LIMITS (Deg.C)

RATING ASME150# FF

CORROSION ALLOWANCE

NONE

MATERIAL STRESS RELIEFCPVC

ITEM NOTES SIZE (NPS) SCH/ RAT END DESCRIPTION COMM CODE

PROJECTS & DEVELOPMENT INDIA LIMITED

SPCL

R2

BC TABLE

REV

Ref.SI Ref.SI

DOC. NO. : PC160/161/EM250 -PDS-600REV.:P

CLIENT :M/S.HURL.

LOCATION :GORAKHPUR(INDIA) .PROJECT :AMMONIA /UREA FERTILIZER PROJECT(OSBL.)

PIPEPIPE 2 - 3 PESCH 80 CPVC,ASTM F441,MF.STD/ASTM F441,PLASTIC PIPE PP552QC00

PIPE 4 - 6 PESCH 80 CPVC,ASTM F441,MF.STD/ASTM F441,PLASTIC PIPE PP552QC00



PIPE 1/2 - 3/4 PESCH 80 CPVC,ASTM F441,MF.STD/ASTM F441,PLASTIC PIPE PP552QC00

PIPE 1 - 11/2 PESCH 80 CPVC,ASTM F441,MF.STD/ASTM F441,PLASTIC PIPE PP552QC00

FLANGEFLANGE 1/2 - 12 FF 150# CPVC,ASTM F441,MF.STD/ASTM F441,SCH80 FL551QC01

BLIND FLANGEBLIND FLANGE 1/2 - 12 FF 150# CPVC,ASTM F441,MF.STD/ASTM F441, BF551QC01

GASKETGASKET 1/2 - 12 3.0 MM THK FF 150# EPDM,MF.STD./ASME B16.21,FULL FACE GS788PA01

STUD & NUTSSTUD & 2NUTS HVY

HEX

- TYPE AB7,, SNFS00000

FITTING (BW)BRANCH WELD WITH

RP

1/2 - 12 PE CPVC,ASTM F441,MF.STD/ASTM F441, WB55JQC00

FITTINGREDUCER CONC. 1/2 - 12 PE CPVC,ASTM F441,MF.STD/ASTM F441, RC55JQC00

REDUCER ECC. 1/2 - 12 PE CPVC,ASTM F441,MF.STD/ASTM F441, RE55JQC00

TEE 1/2 - 12 PE CPVC,ASTM F441,MF.STD/ASTM F441, TE55JQC00

UNION (GJ) 1/2 - 12 PE CPVC,ASTM F441,MF.STD/ASTM F441, UN55JQC00

VALVESGATE VALVE 8 - 12 FF 150# CPVC BODY W/ PP PLUG & EPDM SEATS,GAV500C, GAV500C

CHECK VALVE 1/2 - 12 SOCW 150# CPVC BODY,CHV500C, CHV500C

BALL VALVE 1/2 - 2 SOCW 150# CPVC BODY WITH CPVC BALL,BAV500C, BAV500C

BALL VALVE 3 - 6 FF 150# CPVC BODY WITH CPVC BALL,BAV501C, BAV501C

:

GAV500C :FLANGED GATE VALVE ; 150# ;CPVC BODY(ASTM F441);POLY PROPYLENE PLUG; EPDM SEALS ;TAPERED CYLINDRICAL PLUG DESIGN; BOLTED BONNET; FLAT FACE; FLANGE DIMENSION AS PER ASME B16.1 .

CHV500C :SOCKET WELD CHECK VALVE ; 150# ; H OR V ; UNION OR BOLTED COVER ; BALL TYPE CPVC BODY(ASTM F441);TRIM AS PER BODY MATERIAL ; SOCKET WELD ENDS AS PER ASME B16.11 MANUFACTURER’S STANDARD CONSTRUCTION .

BAV500C :SOCKET WELD BALL VALVE ; 150# ; FLOATING BALL;FULL PORT ;WRENCH OPERATED ; CPVC BODY(ASTM F441);CPVC BALL;VITON O RING SEALS; SOCKET WELD ENDS AS PER ASME B16.11 MANUFACTURER’S STANDARD CONSTRUCTION .

BAV501C : FLANGED BALL VALVE ; 150# ; FLOATING BALL;FULL PORT ;WRENCH OPERATED ; CPVC BODY(ASTM F441);CPVC BALL;VITON O RING SEALS; FLAT FACE; FLANGE DIMENSION AS PER ASME B16.1 ;MANUFACTURER’S STANDARD CONSTRUCTION .

Class: B24RL

PROJECT NO. PC160..162/EM250PIPING MATERIAL SPECIFICATION

SERVICEEFFLUENT,WASTE H2O,CHLORINATED H2O

TEMPERATURE LIMITS (Deg.C)

RATING ASME150# FF

CORROSION ALLOWANCE

NONE

MATERIAL STRESS RELIEFCSRL

ITEM NOTES SIZE (NPS) SCH/ RAT END DESCRIPTION COMM CODE

PROJECTS & DEVELOPMENT INDIA LIMITED

SPCL

R1

BC TABLE

REV

Ref.SI Ref.SI

DOC. NO. : PC161..162/EM250 -PDS-600REV.:0

CLIENT :M/S.HURL.

LOCATION :GORAKHPUR ,BARAUNI,SINDRI (INDIA) .PROJECT :AMMONIA /UREA FERTILIZER PROJECT(OSBL.)

PIPEPIPE 1 - 11/4 PESCH XS CS,SMLS,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PPX721300

PIPE 11/2 - 11/2 PESCH XS CS,SMLS,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PPX721300

PIPE 2 - 21/2 BESCHSTD CS,SMLS,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PPX711300

PIPE 3 - 4 BESCHSTD CS,SMLS,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PPX711300

PIPE 5 - 6 BESCHSTD CS,SMLS,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PPX711300

PIPE 8 - 10 BESCH 20 CS,ERW,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PP2A11300

PIPE 12 - 12 BESCH 20 CS,ERW,API 5L GR.B,NATURAL RBR LND,ASME B36.10,3MM THK LING PP2A11300

FLANGEFLANGE 1 - 2 SO-FF 150# CS,ASTM A105,NATURAL RBR LND,ASME B16.5,3MM THK LING FLX650801

W.N.FLANGE 1 - 12 WN-FF 150# CS,ASTM A105,NATURAL RBR LND,ASME B16.5,3MM THK LING WNX6M0801

SPECL BLIND 1 - 12 FF 150# CS PLT,ASTM A516 GR.60,NATURAL RBR LND,ASME B16.48,3MM THK LING SPX81PO01

BLIND FLANGEBLIND FLANGE 1 - 12 FF 150# CS,ASTM A105,NATURAL RBR LND,ASME B16.5,3MM THK LING BFX610801

GASKETGASKET 1 - 12 FLAT 150# GASKET,SOFT RUBBER,ASME B16.21,3MM THK. GSW190401

STUD & NUTSSTUD & 2NUTS HVY

HEX

- ASTM A193 GR.B7/ASTM A194 GR.2H,, SNDE00000

FITTING (BW)CAP 1 - 12 BW CS,ASTM A234 WPB-SMLS,NATURAL RBR LND,ASME B16.9,3MM THK LING CPX910900

ELBOW 1 - 6 BW CS,ASTM A234 WPB-SMLS,NATURAL RBR LND,ASME B16.9,3MM THK LING ELX910900

ELBOW 8 - 12 BW CS,ASTM A234 WPB-WLDD,NATURAL RBR LND,ASME B16.9,3MM THK LING EL3A10900

REDUCER CONC. 1 - 6 BW CS,ASTM A234 WPB-SMLS,NATURAL RBR LND,ASME B16.9,3MM THK LING RCX910900

REDUCER CONC. 8 - 12 BW CS,ASTM A234 WPB-WLDD,NATURAL RBR LND,ASME B16.9,3MM THK LING RC3A10900

REDUCER ECC. 1 - 6 BW CS,ASTM A234 WPB-SMLS,NATURAL RBR LND,ASME B16.9,3MM THK LING REX910900

REDUCER ECC. 8 - 12 BW CS,ASTM A234 WPB-WLDD,NATURAL RBR LND,ASME B16.9,3MM THK LING RE3A10900

TEE 1 - 6 BW CS,ASTM A234 WPB-SMLS,NATURAL RBR LND,ASME B16.9,3MM THK LING TEX910900

TEE 8 - 12 BW CS,ASTM A234 WPB-WLDD,NATURAL RBR LND,ASME B16.9,3MM THK LING TE3A10900

VALVESGATE VALVE 2 - 12 FLG 150# SS BODY ASTM A351 GR CF8,GAV510, GAV510

GLOBE VALVE 2 - 12 FLG 150# SS BODY ASTM A351 GR CF8,GLV510, GLV510

CHECK VALVE 2 - 12 FLG 150# CS BODY ASTM A216 GR.WCB RUBBER LINED,CHV210D, CHV210D

BALL VALVE 2 - 12 FLG 150# SS BODY ASTM A351 GR CF8M,BAV510, BAV510

BUTTERFLY VALVE 2 - 12 FF 150# CS BODY ASTM A216 GR.WCB RUBBER LINED,BUV203,LUG TYPE BUV203

:

PROJECT NO. PC160/161/EM250 DOC. NO. : PC160/161/EM250 -PDS-600 REV.:0

PROJECTS & DEVELOPMENT INDIA LTD

PC161..162/EM250-PDS-600 0

DOCUMENT NO REV

BRANCH TABLE : TABLE-R1 APPLICABLE PIPING MATERIAL SPECIFICATIONS: B24RL. PRESSURE RATING <= 300#

<-----------------B R A N C H S I Z E------------> 3 1 1 2 1 1 M Q 1 Q M 2 M 3 4 6 8 0 2

M 3Q 1 T 1Q 1M E T 2 E E T 2M 3 E E E T 4 E E E E T 6 E E E E E T 8 E E E E E E T 10 E E P P E E E T 12 E E P P P E E E T

A-

E TE REDUCING TEEP WB BRANCH WELD WITH RPT TE EQUAL TEE

PC160/161/EM250 -PDS-600

A216 GR.WCB RUBBER LINED

DCHV 210D

GRAFOIL/GRAPHITE

GRAFOIL

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