WASTE TREATMENT AND IMMOBILIZATION PLANT CHAPTER 4A ...

WA7890008967 Hanford Facility RCRA Permit Dangerous Waste Portion

Change Control Log Waste Treatment and Immobilization Plant

WASTE TREATMENT AND IMMOBILIZATION PLANT

CHAPTER 4A FIGURES AND DRAWINGS CHANGE CONTROL LOG

Change Control Logs ensure that changes to this unit are performed in a methodical, controlled, coordinated, and transparent manner. Each unit addendum will have its own change control log with a modification history table. The “Modification Number” represents Ecology’s method for tracking the different versions of the permit. This log will serve as an up to date record of modifications and version history of the unit.

Modification History Table

Modification Date Modification Number 09/05/2017 8C.2017.6F

08/2012

WA7890008967 Hanford Facility RCRA Permit Dangerous Waste Portion

Change Control Log Waste Treatment and Immobilization Plant

This page intentionally left blank.

WA7890008967 Waste Treatment and Immobilization Plant

Chapter 4A.1

1

CHAPTER 4A 2 FIGURES AND DRAWINGS 3

4


Chapter 4A.2

1 2

3 This page intentionally left blank. 4

5


Chapter 4A.3

1 CHAPTER 4A 2

ENGINEERING FIGURES 3

4 The figures listed below are included in this chapter, and are to be used in conjunction with the text in the 5 Dangerous Waste Permit (DWP) Chapter 4. 6

7 Figure 4A-1 WTP Simplified Flow Diagram ................................................................................... 5 8

Figure 4A-2 Primary Pretreatment Process Systems ........................................................................ 6 9

Figure 4A-2A Primary Pretreatment Process Systems (Continued) .................................................... 7 10

Figure 4A-3 Primary LAW Vitrification Systems ............................................................................ 8 11

Figure 4A-4 Primary HLW Vitrification Systems ............................................................................ 9 12

Figure 4A-11 Cesium Resin Addition Process System (CRP) ......................................................... 10 13

Figure 4A-21 LAW Melter Process System (LMP) ......................................................................... 11 14

Figure 4A-24 LAW Container Finishing Handling System (LFH) .................................................. 12 15

Figure 4A-27 HLW Melter Process System (HMP) ......................................................................... 13 16

Figure 4A-38 Typical Tank System – Cesium Ion Exchange Column ............................................. 15 17

Figure 4A-48 Typical System - LAW Melter Process System (LMP) ............................................. 17 18

Figure 4A-53 Typical Tank System – HLW Melter Feed Process System (HFP) ........................... 18 19

Figure 4A-59 Typical System - Containment Building (Sheet 1) ..................................................... 19 20

Figure 4A-59 Typical System - Containment Building Typical Design Features Crosswalk 21 (Sheet 2) ..................................................................................................................... 21 22

Figure 4A-65 Simplified General Arrangement Pretreatment - Plan at El. 98 ................................. 25 23

Figure 4A-118 Schematic of an Example IHLW Container and Label .............................................. 26 24

Figure 4A-119 Schematic of an Example ILAW Container and Label .............................................. 27 25

Figure 4A-120 Typical Arrangement of a Reverse Flow Diverter ..................................................... 29 26

Figure 4A-121 Basic Reverse Flow Diverter Design ......................................................................... 31 27

Figure 4A-122 Typical Arrangement of a Steam Ejector System ...................................................... 33 28

Figure 4A-123 Typical Seal Pot Arrangement ................................................................................... 34 29

Figure 4A-124 Typical Breakpot Arrangement .................................................................................. 35 30

Figure 4A-127 Typical Bulge Configuration ...................................................................................... 36 31

Figure 4A-128 Typical Primary Containment Sump Conceptual Design........................................... 37 32 33


Chapter 4A.4

1 2 3

This page intentionally left blank. 4 5


Chapter 4A.5

1

Figure 4A-1 WTP Simplified Flow Diagram 2 3

.... .. ............... . .... .. '.' ' ''''' ' .. .. ... . ........................... .. ... ·. · ............... . ....... ..... '''' ' . ' . ' . ' . .. .... .. .. :

Pretreatment Pia nt

Condensale 1--------c<,,oet...::<----r---~ to U:RFIETF

LAWFeed1-....,.==-~ Cewm

Concentrnles

HLW Blending Vessel

I.letter Feed Preparation

PT

S™*

HLW Vitrification Plant

.__""_:._·_i:-_"_'PI_• __ ? •• .------••

S1-S3:,q>ltPON 1 S?- SitrO)f Port2 AgM · $8.li'i l.~ r; r,e ET1" •E.'11.itntTfUnltrlflCCJ rif)/.E" -~~C'/ J.'S: Dnl"IIXlf M!PA -1gl~C, Pt10..tl2Nl .-4tr ,._w - ~41!vth ,u~ I.AW · L0'#-3d~WU~ LE!v . uc,g,c, e:::,,IOlC'9CIOll foctlJ

HlWSuck

PJl.4 •AIM Jt1 llt:tt Plfl) • !\NtM fO'# Oliffltf ses -Sit.wn~cetoScr.botr SCft - St~e QU;tJO:ReOJctb'I TCO - 1brn111 c.aa-,,oeoxa¥.10n Wf.Sf> • Wftf~tiCPtlObD»r . l\?$-lOW-Aa\flJ 11\'IRtPJf:UVN-C S/ Qt~ :

Evaporator f ... ' . . .. .. .. .. .. · . ... . . .. ........ .. . ... ' ... . .... ·.· ......... . .... ........ '.'

_ ........................ !

LAW and HLWFeed

Rece,pt

LAWt.leler Feed

Evaporator

Cs Ion Exchange

LAW Glass Formers& Reductants

LAWPS Condensale

to El.IF

Effluent Management Facility

Condensate to U:RFIETF/


Chapter 4A.6

1

Cs ConcentrateCNP-VSL-00003

DOETankFarms

Pretreatment HE

A

HE

A

LAW FeedReceipt Vessel

FRP-VSL-00002A/B/C/D

HLW FeedReceipt Vesse

HLP-VSL-00022

Waste FeedEvaporator

Feed VesselFEP-VSL-00017A/B

UltrafiltrationFeed

PreparationVessel

UFP-VSL-00001A/B

UltrafiltrationFeed VesselUFP-VSL-00002A/B

PermeateHoldingVessels

UFP-VSL-00062A/B/C

Waste FeedEvaporatorCondensate

VesselFEP-VSL-

00005

HLW LagStorage Vessel

HLP-VSL-00027A/B

HLW FeedBlend Vessel

HLP-VSL-00028

Plant WashVessel

PWD-VSL-00044

Acidic/AlkalineEffluentVessel

PWD-VSL-00015

Acidic/AlkalineEffluentVessel

PWD-VSL-00016

FEP-COND-00001A/B

FEP-COND-00002A/B

FEP-COND-00003A/B

UFP-FILT-00001A/B

UFP-FILT-00002A/B

UFP-FILT-00003A/B

Waste FeedEvaporator

VesselFEP-SEP-00001A/B

CausticScrubber

PVP-SCB-00002

PVP-HTR-00001A/B/C PVP-HEPA-

00001A/B/CPVP-HEPA-00002A/B/C

PVP-HEME-00001A/B/C

Waste FeedEvaporation

(System FEP)

HLW Lag Storage andFeed Blending

Process(System HLP)

PretreatmentEffluent

Collection(System PWD)

PT Vessel Vent(PVP/PVVSystems)

LAW Ultrafiltration(System UFP)

LAW Feed Receipt(System FRP)

Cleaning Reagents

Process Condensate

Process Condensate Vessel Vents

Blended HLW Feedto HLW VIT

HLW SBS Purge &Canister Decon

Process CondensateRLD-VSL-00006A

LAW Plant Wash

Process Condensatefrom CNP

Dilute Effluent fromCs Ix

Permeate to Cs IXCXP-VSL-00001

To VOC Oxidation /Carbon Bed Adsorber /

Stack

DoubleShellTank

HLW Feed Receipt(System HLP)

Chemical Additives

HE

A

HE

A

Stack

PJV-DMST-00002A/B/C

Demister

HEPAsA/B

Exhaust FansA/B/C

RFD/PJM Exhausts

PVP/PVV System

UFP-FILT-00004A/B

UFP-FILT-00005A/B

PT Pulse Jet Ventilation(PJV System) 2

Figure 4A-2 Primary Pretreatment Process Systems 3

o- -, ~- -o I I I I I I I I e ll

0 ~: : I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I I

O-- .J L- -O

I ---


Chapter 4A.7

TLP-COND-00001

TLP-COND-00003

TLP-COND-00002

reated LAWEvaporator

VesselTLP-SEP-

00001

Cs IX FeedVessel

CXP-VSL-00001

Cs IonExchangeColumn

CXP-IXC-00001/2/3/4

Treated LAWCollection

VesselCXP-VSL-

00026A/B/CLAW

ConcentrateStorage Vessel

TCP-VSL-00001

LAW SBSCondensate

Receipt VesseTLP-VSL-00009A/B

reated LAWEvaporatorCondensate

VesselTLP-VSL-

00002

Process CondensateVessel

RLD-TK-00006A

Process CondensateVessel

RLD-TK-00006B

AlkalineEffluentVessel

RLD-VSL-00017A/B

CsEvaporator

ConcentrateLute Pot

CNP-VSL-00002

RecoveredAcid TankCNP-VSL-

00004

Cs EvaporatorSeparator

CNP-EVAP-00001

Cs After CondenserCNP-HX-00003

Cs PrimaryCondenser

CNP-HX-00002

Cs RectifierColumn

CNP-DISTC-00001

CNP-HX-00001

Radioactive Liquid Disposal(System RLD)Cs Nitric Acid

Recovery(System CNP)

Cesium IonExchange

(System CXP)

Treated LAWEvaporation

(System TLP/TCP)

Condensate fromFEP-VSL-00005

LAW Concentrate toLAW VIT

LAW SBS PurgeRLD-VSL-00005

Dilute Effluents toPWD-VSL-00015/16

Permeate from UFP-VSL-00062 A/B/C

Low Active Effluentto LERF/ETF

Cs Concentrate to HLP-VSL-00028

Condensate to PWD-VSL-00015/16

Process CondensateRecycle to PT

Caustic Effluent fromLVP-VSL-00001

Future AlternativeLAW Process

PVP/PVV System

1 2

Figure 4A-2A Primary Pretreatment Process Systems (Continued) 3

---------~ .... , ___ _,.


Chapter 4A.8

1 2

Figure 4A-3 Primary LAW Vitrification Systems 3

o- - :- ----, ~ '""° ! --""-,.-.... -•• ~:,--------------------------, ~ ,...__ _ __, LAW Melter Concentrate

j r,1:liirrc;;;;;nk-+l ___ __:R,::e:::c:::.e·:!,p::t.:&:..:P~r.::e~pa::r.:a::;tion Process (System LCP /LFP)

LAW Facility

0-o ____ _

LAW Melter Offgas Treatment(System LOP /LVP)

LV......OC.•O0OC>1 l~'!~ l~! lVP-sa-oo00J t.VP..SCMJOOOZ

Stet:


Chapter 4A.9

HMP-MLTR-00001HMP-MLTR-00002

Film CoolersHOP-FCLR-00001HOP-FCLR-00002

Glass FormerFeed Mixer

HLW MelterFeed Prep

VesselsHFP-VSL-00001-00005

Carbon BedAdsorber

H0P-ADBR-00002A/2B

SBSCondensate

VesselsHOP-VSL

-00903-00904

SBS ColumnsHOP-SCB-00001HOP-SCB-00002

WESPsHOP-WESP-00001HOP-WESP-00002

Stack

HLW MelterOffgas Treatment(System HOP)

HLW Melter ConcentrateReceipt & Preparation

Process (System HCP/HFP

Canisters

HLW MelterFeed

VesselsHFP-VSL-00002-00006

Pret

reat

men

t Fac

ility

Bala

nce

of F

acili

ties

HLW Facility

To PretreatmentPWD-VSL-00043

HydrogenPeroxide

HE

A

HE

A

HE

A

HE

A

TCO/SCR SkidsHOP-SKID-00005HOP-SKID-00007

AcidWasteVessel

RLD-VSL-00007

Note. 1 OffgasDrainsVessel

RLD-VSL-00002

2 MHNO3

CanisterDeconTank

HDH-VSL-00002-00004

Air Sparge

NeutralizationTank

HDH-VSL-00003

Air Sparge

H2O

Ceric Nitrate

HLW Melters

Plant Washand Drain

VesselRLD-VSL-

00008

Product CanisterDecontamination

(System HDH)

HeatExchanger

Vessel VentHeader

HEME

HEME

HOP-HEME-00001A/B

HOP-HEME-00002A/B

SilverMordeniteColumn

HOP-ABS-00002

HOP-ABS-00003

CanisterDeconBogieVessel

BoosterExtraction

Fans

StackExtraction

Fans

Pulse VentHeaders

HEPAs

HEPAs

ElectricHeater

HE

A

ElectricHeater HEPAs Extraction

Fan

Ammonia

ElectricHeater

HLWConcentrate from

Pretreatment

HDH-VSL-00001

To PretreatmentPWD-VSL-

00033/00043

1 2

Figure 4A-4 Primary HLW Vitrification Systems 3

11 11

~ -- 11 o- - _-_-___ .JI 11 11 11 11

11 11 11 11 11 11 11 11 11 1--11 r===__J ___ _

I 11r===-'---~

I 1--- 1 ---

11 11 11 11

__ I


Chapter 4A.10

SpentResinSlurryVessel

Cs ResinAdditionAir GapVessel

Cesium Resin AdditionProcess System (CRP)

Cs ResinAdditionVessel

Cs IonExchangeColumns

1

Resin / Caustic

Sodium Hydroxide

Demineralized WaterFresh Resin

Process Condensate toWaste Feed Evaporator

2

Caustic

Nitric Acid

Spent Reagents toRLD-VSL-00017A/B

Resin / Caustic

4

3

CXP-IXC-00001, CXP-IXC-00002,CXP-IXC-00003, CXP-IXC-00004are part of system CXP.Included here for clarity.

Legend

LiquidSlurry

1

2 RDP-VSL-0002A is a part of systemRDP. Included here for clarity.

3 CRP-VSL-00001

4 CRP-VSL-00002

1 2

Figure 4A-11 Cesium Resin Addition Process System (CRP) 3

c:::>

c:::> c:::> c:::>

L--·-·-·-·-·-·-·-·-·-·-·-·-·-·-,

c:::>


Chapter 4A.11

LAW MelterProcess System

LAW Locator: LMP

Pressure Control Air

Process Air

Sparge Bubbler Air

Air in - Leakage fromMelter Enclosure

Low Pressure Steam

Process Figure

Liquid

SlurryGas

Legend

Solid

Film CoolerLOP-FCLR-1/3

Primary

( Note 2 )

LAW Melter

ContainerContainer

Notes:1.There are 2 melters LAW-MLTR-00001/2 each with a dedicated feed vessel and submerged Bed Scrubber.2.Each Melter has a Primary ( LOP-FCLR-00001/3 ) and a Standby (LOP- FCLR-00002/4 ) Film Cooler.3.Glass is poured from discharge chambers to containers one at a time in an alternating sequence.

Film CoolerLOP-FCLR-2/4

Standby

( Note 2 )

See Note 1

To Submerged Bed Scrubber

To Submerged Bed Scrubber

Instrument Air

LAW Blended Melter Feed (6 nozzles feedmelter LFP VSL00002/4)

Note 3Note 3

1 2

Figure 4A-21 LAW Melter Process System (LMP) 3

,..__ ______ •------------------------------------------------------------• ' ' ' ' '

---------------------------------~L-____ ____...

~' ==========•----------------------------------------------------------.-n .__I ____ ____,•-----------------------------------------------------------.y

r-----.j ________ •

.___ _____ ..... . - . - . - . - . - . - . - _____________ !

....____ ___ • ---------------------------------------:

~------------------------------: l ._ ______________ _.,_ ' '

' '

•---------------------· ! l .______ : t . , 0 ..........................

• II


Chapter 4A.12

Decon Air Dryer

Decon CO2 Pelletizer

Decon Offgas to FacilityVentilation System

Liquid CO2 supply from bulktransport truck

DeconCompressed Air Storage

DecontaminationBooth

HEPA

Vacuum Pump

Decon AirCompressorRoom Air

Decon AirAftercooler

DeconCO2

Storage

Liquid

CO2 PelletsGas

Legend LAW Container FinishingHandling System (LFH)

1 2

Figure 4A-24 LAW Container Finishing Handling System (LFH) 3

~I~~ ~--·- ·1 .. -------------• I •-------------- . : I

r:::_ - ································:~·- - - -

lil'il''lli

:···' • ~ r

= -======--=Ll>--------------~L----1 ===-----

---------· t=t=======--==~--==-=-=il>


Chapter 4A.13

HLW MelterProcess System

HLW Locator HMP

Pressure Control Air

Film Cooler Air

Sparge Bubbler Air

Air in - Leakage(from Melter Cave)

HLW Blended Melter FeedHFP-VSL-00002/6

Process Figure

Liquid

SlurryGas

Legend

Solid

Film CoolerHOP-FCLR-00001/2

PrimaryNote 2

HLW MelterCanister Canister

To Submerged Bed Scrubber HOP-SCB-00001

Instrument Air

Note 3 Note 3

See Note 1

Notes:1.There are two Melters, HLW-MLTR -00001/2, each with a dedicated Melter Feed Vessel and Submerged Bed Scrubber2 Each HLW Melter has one Film Cooler and one standby.3.Glass is poured from discharge chambers to containers one at a time, in alternating sequence.

1 Figure 4A-27 HLW Melter Process System (HMP) 2

3

............................................................................. ! _____ _J. • ,············-······j

------------------•·····---------·········---------· iJi r------.__ _____ ........ __ _ _

~ - ·- · - · - ·

11:=1 ========~ .. ·····································i ~========~::::::::::::::::::::::~········1 i r······················J

. ' + ! =


Chapter 4A.14

1 2

3 This page intentionally left blank. 4

5


Chapter 4A.15

1 Figure 4A-38 Typical Tank System – Cesium Ion Exchange Column 2

3

Vapor Space Vessel Wash Reagents

Resin Addition

LAW Addition

reated LAW to Process

Spent Resin

Vessel Vent

Drain to Recycle

Supports

Hot Cell Wall

Wa l Penetrations

L L

Level Measurement Steam Ejector

Screen

Rad Monitor

High High emp

Interlock

Ch lled Water Supply

Chil ed Water Return

Wa l Penetration

Wall Penetration

Purge Air Resin F ush

Screen

Sta nless Steel Liner and/ or Protective Coat ng

Construction oint

Typical Tank System - Cesium Ion Exchange Column

Protective Coat ng

,,

\ ...


Chapter 4A.16

1 2 3



Chapter 4A.17

1 2

Figure 4A-48 Typical System - LAW Melter Process System (LMP) 3

Refractory

Plenum

Cold Cap

Melt Pool

Heating Electrode

0 0

0 0

Feed

6

Melt Pool

Not to scale

Airlift

Plenum

Discharge Throat

Q

0

a

Glass Container

Discharge Chamber

Discharge Trough

Airlift Riser


Chapter 4A.18

1 2

Figure 4A-53 Typical Tank System – HLW Melter Feed Process System (HFP) 3

HFP System Typical Vessel Single Wall Stainless Steel

Transfer Devices

Stainless Steel Liner and/or Protective

Coating

HLW Concentrate

Wall Penetration

Stainless Steel Single Wall Piping

Concrete Cell Wall

Construction Joint between Liner and Concrete Wall

High Level Alarm

Typical Sump

Steam Ejector

Protective Coating On Concrete

Supports

L

Level Measurement

To HLW Melter

High High Level Trip

Low Level Alarm

To HLW RLD System

Glass Formers

Typical Tank System - HLW Melter Feed Process System (HFP)

l

•-


Chapter 4A.19

1 Figure 4A-59 Typical System - Containment Building (Sheet 1) 2

3

Shield Windows(Sealed)

MSM Penetrations(Sealed)

Through Wall Drives(Sealed)

Container

Rotate Stand

In - CellCrane

Grab

Container

SwabbingMachine

SwabContainer

SwabContainer

HighActive

Swab entry point

Steel-reinforcedConcrete Walls andCeilings

Stainless SteelLiner and/orProtective Coating

Steel-reinforcedConcrete Foundation

Welded Seam

Welded Seam

Sealed ConstructionJoint

To HEPA Filtration

Airflow Directionto MaintainNegativePressure

Import and ExportHatches with Air FlowSeals

Shield Door

Air Flow Direction Containment

Typical System - Containment Building

I i.,.,:·····.:: . .···:··~·-.:,:.·rv .. ,: ~-. 1-.;·:::::::::::::::::i ·- :·· ..

c::============~: t::::::=::• ===================1, i .. £ / i/

•.

1 ~-- .lL ,, _J, 12r·-l::::1 n······n ,.:.-.-

11 ........................... n:r

1~[ .............. -...... J ......... r::r::: :::::::J

r_LL ...... Ll.1 l l _ :--: _.--=

.....-------,-··---------------------· ~·- (______.___________,r···· L. ..... ...l ····: • ..,____----! ........... i··i·······'

.........._ __ i:::::::----,=il:---~\.. ........ -.. 1 ......

I

\


Chapter 4A.20

1 2 3



Chapter 4A.21

Figure 4A-59 Typical System - Containment Building Typical Design Features Crosswalk 1 (Sheet 2) 2

Containment Building Neg

ativ

e Ce

ll A

ir Pr

essu

re

Air

Flow

to H

EPA

Filt

ers

SS L

iner

With

Wel

ded

Seam

s

Impo

rt / E

xpor

t Hat

ch -

(Con

trolle

d A

ir G

ap)

Shie

ld W

indo

ws -

(Sea

led)

Stee

l Rei

nfor

ced

Con

cret

e Fl

oor/F

ound

atio

n

Stee

l Rei

nfor

ced

Con

cret

e W

alls

& C

eilin

gs

Thro

ugh

Wal

l MSM

s - (S

eale

d)

In -

Cell

Brid

ge C

rane

/ M

onor

ail

Hor

iz./V

ertic

al S

hiel

d D

oors

- (C

ontro

lled

Air

Gap

)

Misc

ella

neou

s In-

cell

Room

Equ

ipm

ent

Pretreatment Plant Pretreatment Hot Cell Containment Building (P-0123) X X X X X X X X X X X Pretreatment Maintenance Containment Building PM0124 Hot Cell Crane Maintenance Mezzanine X X X X X X P-0121A Spent Resin Dewatering X X X X X X X P-0122A Waste Packaging Area X X X X X X X P-0123A Remote Decontamination Maintenance Cave X X X X X X X X X P-0124 C3 Workshop X X X X X X X X P-012C1 C3 Workshop X X X X X X X X P-0125 Cask Lidding Airlock X X X X X X X X P-0125A Cask Lidding Room X X X X X X X X P-0128A MSM Repair Area X X X X X X X P-0128 Temporary Storage Room X X X X X Pretreatment Spent Filter Drum Handling Area Containment Building (P-0223) X X X X X X Pretreatment Filter Cave Room Containment Building (P-0335) X X X X X X X Pretreatment PJV Secondary HEPA Filter Room Containment Building (P-0431A) X X X X 3


Chapter 4A.22


ativ

e Ce

ll A

ir Pr

essu

re

Air

Flow

to H

EPA

Filt

ers

SS L

iner

With

Wel

ded

Seam

s

Impo

rt / E

xpor

t Hat

ch -

(Con

trolle

d A

ir G

ap)

Shie

ld W

indo

ws -

(Sea

led)

Stee

l Rei

nfor

ced

Con

cret

e Fl

oor/F

ound

atio

n

Stee

l Rei

nfor

ced

Con

cret

e W

alls

& C

eilin

gs

Thro

ugh

Wal

l MSM

s - (S

eale

d)

In -

Cell

Brid

ge C

rane

/ M

onor

ail

Hor

iz./V

ertic

al S

hiel

d D

oors

- (C

ontro

lled

Air

Gap

)

Misc

ella

neou

s In-

cell

Room

Equ

ipm

ent

LAW Vitrification Plant LAW LSM Gallery Containment Building (L-0112) X X X X X X ILAW Container Finishing Containment Building L-0109B Swabbing Cell North Line X X X X X X X X X X L-0109C Decontamination Area North Line X X X X X X X X X X L-0109D Inert Fill / Welding Area North Line X X X X X X X X X X L-0115B Swabbing Cell South Line X X X X X X X X X X L-0115C Decontamination Area South Line X X X X X X X X X X L-0115D Inert Fill / Welding Area South Line X X X X X X X X X X L-0109E Container Monitoring/Export Area - North Line X X X X X X X X X X L-0115E Container Monitoring/Export Area - South Line X X X X X X X X X X LAW Vit Plant C3 Workshop Containment Building (L-226A) X X X X X X LAW Consumable Import/Export Containment Building (L-0119B) X X X X X X LAW Pour Cave Containment Building L-B015A Pour Cave (Melter 1) X X X X X X X X X X L-B013C Pour Cave (Melter 1) X X X X X X X X X X L-B013B Pour Cave (Melter 2) X X X X X X X X X X L-B011C Pour Cave (Melter 2) X X X X X X X X X X L-B011B (Spare) X X X X X X X X X X L-B009B (Spare) X X X X X X X X X X ILAW Container Buffer Storage Containment Building

L-B025C L-B025D

1


Chapter 4A.23


ativ

e Ce

ll A

ir Pr

essu

re

Air

Flow

to H

EPA

Filt

ers

SS L

iner

With

Wel

ded

Seam

s

Impo

rt / E

xpor

t Hat

ch -

(Con

trolle

d A

ir G

ap)

Shie

ld W

indo

ws -

(Sea

led)

Stee

l Rei

nfor

ced

Con

cret

e Fl

oor/F

ound

atio

n

Stee

l Rei

nfor

ced

Con

cret

e W

alls

& C

eilin

gs

Thro

ugh

Wal

l MSM

s - (S

eale

d)

In -

Cell

Brid

ge C

rane

/ M

onor

ail

Hor

iz./V

ertic

al S

hiel

d D

oors

- (C

ontro

lled

Air

Gap

)

Misc

ella

neou

s In-

cell

Room

Equ

ipm

ent

HLW Vitrification Plant HLW Melter Cave 1 Containment Building: X X X X X X X X X X X H-0117 Melter Cave 1 X X X X X X X X X X X H-0116B Melter Cave 1 - C2/C3 Airlock X X X X X H-0310A Melter Cave 1 Equipment Decon Pit X X X X X X X X X X HLW Melter Cave2 Containment Building: X X X X X X X X X X X H-0106 Melter Cave 2 X X X X X X X X X X X H-0105B Melter Cave 2 - C2/C3/ Airlock X X X X X X 1 H-0304A Melter Cave 2 Equipment Decontamination Area X X X X X X X X X X IHLW Canister Handling Cave Containment Building (H-0136) X X X X X X X X X X X

IHLW Canister Swab and Monitoring Cave Containment Building (H-0133) X X X X X X X X X C3 Workshop Containment Building: X X X X X C3 Workshop (H-0311A) X X X X X C3 MSM Maintenance Workshop (H-0311B) X X X X HLW Filter Cave Containment Building (H-0104) X X X X X X X X X X HLW Waste Handling Area Containment Building: X X X X H-0410B E&I Room X X X X H-0411 Waste Handling Room X X X X HLW Pour Tunnel 1 Containment Building (H-B032) X X X X X X X HLW Pour Tunnel 2 Containment Building (H-B005A) X X X X X X X HLW Drum Swabbing and Monitoring Area Containment Building: X X X X X H-0126A Crane Maintenance Room X X X X H-0126B Swabbing and Monitoring Room X X X X H-B028 Cask Import/Export Room X X X X X 1 2


Chapter 4A.24

1 2 3



Chapter 4A.25

1 Figure 4A-65 Simplified General Arrangement Pretreatment - Plan at El. 98 2

Some information, on this page, may appear to be illegible; however, the information necessary for assuring adequate design is legible 3

---

0

C

-.,'C.

,,

r,

Ptll'lU,. Pl~II ,:' l. (L 11!1 ~t,

~b .,.,.,.,.~=-=-· ::r

•

,, _:r

:..."-

J ) r

..... .,. ttl.lRW)) PA· flM.. F\_.111( '8" ,,.-r £t ts'·O"

• •

Ld=,, ~

...... J "1))0

.•.

,i,1'1111. •JTU, '---'==-----I ,..., ________ G

~,,,.a'"" _____ _

. ~.,;:::-'-----·-. --~ !?~~1."J$9~~-

1= -

----·· --~---·-----·--------·-----____ ....,,. ____ _ :;-;~·-·· ..... J

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·-----·--... --·--...... ..

~-------.~"!'"~"."~"_"_,..,..._ ;cl.~

---

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•


Chapter 4A.26

1 Figure 4A-118 Schematic of an Example IHLW Container and Label 2

Some information, on this page, may appear to be illegible; however, the information necessary for assuring adequate design is legible 3

CD HLW CANISTER DETAIL

DETAILK SCALE: 1:2

(APPLIES 2 PLACES) CANISTER NUMBER

SANS SERIF HELVETICA CMEGARON) MEDIUM FULL WIDTH TYPICAL IDENTIFICATION WELD

SEE 24590-HLW-MX-30-00010001

AND 24590-HLW-MX-30-00010003

VIEW J-J SCALE= NTS

1- SEE DETAIL K I

I

R 9.125 :!:.250


Chapter 4A.27

1 Figure 4A-119 Schematic of an Example ILAW Container and Label 2

Some information, on this page, may appear to be illegible; however, the information necessary for assuring adequate design is legible 3 4

7 A

_l_.080A

"'"" JJ )' xxxxx

.. ,,ll '-.12

2.00 .00

1.40 00

DETAIL SCALE-½"- 7

CONTAINEEiANRUOMNBEJEoT1i~lC/&LL2xWIDTH SANS SERIF M

VIEW A-A SCALE, 1/~" = 7"

SECTION B-B SCALE:½"- 1"


Chapter 4A.28

1 2 3



Chapter 4A.29

RFD CONTROLSYSTEM

PI

PT PT

compressedair/gas

‘Y’ typestrainer

pressureregulator

pressure indicator

primary automaticisolation valve

secondary automaticisolation valve

needle valve

pressure transducer

manual isolation

‘Y’ type strainer

suction/drive jet pump pair

charge vessel

RFD

to deliveryvessel

supply vessl

A B

0300.doc

1 Figure 4A-120 Typical Arrangement of a Reverse Flow Diverter 2

Some information, on this page, may appear to be illegible; however, the information necessary for assuring 3 adequate design is legible 4 5


Chapter 4A.30

1 2 3



Chapter 4A.31

BASIC RFDDESIGN

Inlet Nozzle Outlet Nozzle

0050 v002.vsd 1

Figure 4A-121 Basic Reverse Flow Diverter Design 2

3

1,; \..'"

~ r ~ \..._

·------------ - ------ -- ------------I

" I r I ~ -I \... I I

I

I


Chapter 4A.32

1 2 3



Chapter 4A.33

STEAMSUPPLY

VENT AIRSUPPLY

ACTUATOR

3 WAY VALVE

TO CELL ORVESSEL VENT

SYSTEM

TO OTHERVALVES

NRV

STEAM VALVE CABINET

C2 ORC3 AREA

40 mm - 50 mm n.b.

25 mm n.b. 15mmn.b.

Backupconnection

MINIMUM HEIGHTTO BE AT LEAST 1

BAROMETRICHEAD OF FLUID

ABOVE A LIFT ANDFORCE EJECTOROR THE MAXIMUM

FLUID LEVEL INTHE SUPPLY

VESSEL FOR ASUBMERGED

EJECTOR

BREAKPOT

DELIVERY VESSEL

VENTSYSTEM

VENT SYSTEM

SUPPLY VESSEL

HIGHEST DISCHARGE POINT

VENT SYSTEM

C4 OR C5 CELL

TYPICALARRANGEMENT OF A

STEAM EJECTORSYSTEM

STEAM SUPPLY PIPE

EJECTORDELIVERY PIPE

EJECTORSUCTION PIPE

END OF SUCTION PIPEOR MIN MUM FLUID

LEVEL

BREAK POTDISCHARGE PIPE

ALTERNATIVESUBMERGED

EJECTOR

LIFT ANDFORCE

EJECTOR

OVERFLOW

VAC. BREAKVALVE

Needle valve lockedopen to assure in-bleed

on failure of vent airsupply air

0051 v002.vsd 1 Figure 4A-122 Typical Arrangement of a Steam Ejector System 2

3


Chapter 4A.34

1 Figure 4A-123 Typical Seal Pot Arrangement 2

3

VENT

FEED

VENT

SEAL

SEAL POT


Chapter 4A.35

1 2

Figure 4A-124 Typical Breakpot Arrangement 3

VESSEL SUPPORT

VESSEL VENT

PROCESS OUTLET

DISENTRAINMENT (PACKED) SECTION

PROCESS INLET

OVERFLOW

0052 v002.ppt


Chapter 4A.36

1 Figure 4A-127 Typical Bulge Configuration 2

3

,_-\ 'mt flller

(T•p Vk"')

.......

(Sldt Vkw)


Chapter 4A.37

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34

Figure 4A-128 Typical Primary Containment Sump Conceptual Design 35

A A

SECTION A-A

B B

SECTION B-BSECONDARYSUMP(EXSTING)

PRIMARYSUMP

D D

Leak Detection Probe

Primary Sump

Secondary Sump


Chapter 4A.38

1 2 3


WASTE TREATMENT AND IMMOBILIZATION PLANT CHAPTER 4A ...

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