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1 1 Presented by: Delmar Noyes, Acting Assistant Manager for WTP Startup, Commissioning and Integration Oregon Hanford Cleanup Board Agency Update August 7, 2017

Agency Update - oregon.gov · BNI is responsible for the engineering, construction, startup and commissioning of ... (MARS) Sluicing Retrieval System (MARS) Vacuum Retrieval Methodology

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Presented by:

Delmar Noyes,

Acting Assistant Manager for WTP Startup, Commissioning and Integration

Oregon Hanford Cleanup Board

Agency Update

August 7, 2017

2

MissionTo safeguard the nuclear waste

stored in Hanford’s 177 underground

tanks, and to manage the waste

safely and responsibly until it can be

treated in the Waste Treatment and

Immobilization Plant for final

disposition.

VisionTo be a high-performing, innovative

organization that is safety-

conscious and employee-focused,

and committed to achieving our

mission with environmental and

fiscal responsibility.

3

Office of River Protection (ORP)ORP is responsible for planning, integrating,

and managing the River Protection Program

executed by contractors performing work

under ORP management. ORP has ~225

employees, both federal and contractor.

Washington River

Protection Solutions (WRPS)WRPS is the prime contractor responsible

for safely managing and operating the Tank

Farms. WRPS has 2,134 employees*.

Bechtel National, Inc. (BNI)BNI is responsible for the engineering,

construction, startup and commissioning of

the Waste Treatment and Immobilization

Plant. BNI has 2,913 employees*.

Wastren Advantage, Inc. (WAI)WAI is the prime contractor responsible for

managing the 222-S Laboratory. WAI has 54

employees.**As of March 31, 2017

Our Team

4

5

Effluent Treatment

Facility Ponds

River Protection Project

6

Tank Farms Update

6

7

1 TANK UNDER REVIEW16 TANKS RETRIEVED

1 TANK IN RETRIEVAL

4 TANKS PREPARING FOR RETRIEVAL

Hanford Tank Cleanup Status

Enhanced Reach

Sluicing System

(ERSS)

+ High-Pressure Water

Remote

Water Lance

(Salt Mantis)

Mobile

Retrieval Tool

(Foldtrack)

High-Pressure

Mixer

(Rotary Viper)

Mobile Arm

Retrieval System

(MARS)

Sluicing

Mobile Arm

Retrieval System

(MARS)

Vacuum

Retrieval

Methodology

Key

241-S-112 and 241-S-102 Phase 1

241-SY-102

Water SupplyWater

Distribution

SkidFrom SY Farm

Sludge

Saltcake Working Solution

241-S-Farm

Supernate

Solids

Riser

ExtensionDistribution

Pit

Recirculation

Drop LegRaw Water

Dilution

LineRaw Water

Distribution

Devices

241-S-A

Valve Pit

ASSD

R-7

R-14R-13R-6R-16R-11

241-S-112 and 241-S-102 Phase 1

241-SY-102

Water SupplyWater

Distribution

SkidFrom SY Farm

Sludge

Saltcake Working Solution

241-S-Farm

Supernate

Solids

Riser

ExtensionDistribution

Pit

Recirculation

Drop LegRaw Water

Dilution

LineRaw Water

Distribution

Devices

241-S-A

Valve Pit

ASSD

R-7

R-14R-13R-6R-16R-11

Raw Water

Ambient Air

Ambient Air

Water Supply Skid

Air Compressor Skid

InletHEPAFilter

NESLUtilityBox

Hydraulics

CCTV

PDIT

High Pressure

Low PressureAll

Systems

Flush

AMSSpacer

Drain

AMS

Drain

Vacuum

Pump

Vacuum

Pump

Seal Water

Separator

Vacuum Skid

Vessel Pump Skid

Drain

Hydraulics

Waste Slurry

to 241-AN-106

Atmosphere

Portable Exhaust Poro 3

Transfer

PumpSlurry

Tank

Hydro-

trans

R-5 R-6 R-7 Diversion Box

Vacuum

Exhaust

EXH-1001-HIH

air

water

waste

vacuum/exhaust

hydraulics

Raw Water

Ambient Air

Ambient Air

Water Supply Skid

Air Compressor Skid

InletHEPAFilter

NESLUtilityBox

Hydraulics

CCTV

PDIT

High Pressure

Low PressureAll

Systems

Flush

AMSSpacer

Drain

AMS

Drain

Vacuum

Pump

Vacuum

Pump

Seal Water

Separator

Vacuum Skid

Vessel Pump Skid

Drain

Hydraulics

Waste Slurry

to 241-AN-106

Atmosphere

Portable Exhaust Poro 3

Transfer

PumpSlurry

Tank

Hydro-

trans

R-5 R-6 R-7 Diversion Box

Vacuum

Exhaust

EXH-1001-HIH

air

water

waste

vacuum/exhaust

hydraulics

241-C-106 241-AN-106

Water Supply

Acid/Water/Air Supply

Pump Skid

Sluice Pit

241-AY-02E

Sluice Pit

241-AY-06C

Heel Pit

241-AY-06B

Sluicer Mixing

Eductor

Pump

Central Pump Pit

241-AN-06A

Caustic Supply

(by others)

OGT

OGT

Mixer

Pump

R-3AR-13

R-7R-3 R-13

241-C-106 241-AN-106

Water Supply

Acid/Water/Air Supply

Pump Skid

Sluice Pit

241-AY-02E

Sluice Pit

241-AY-06C

Heel Pit

241-AY-06B

Sluicer Mixing

Eductor

Pump

Central Pump Pit

241-AN-06A

Caustic Supply

(by others)

OGT

OGT

Mixer

Pump

R-3AR-13

R-7R-3 R-13

241-C-100 Tanks DST

Sluicer

#1

Sluicer

#2Slurry

Pump

Supernatant

Pump

Portable

Valve Pit

High Pressure

w ater skid

Hy draulic pow er

pack

Rotates

High Pressure

Lance Head

Height

Adjustable

Riser

Acid Dissolution Vacuum Retrieval Saltcake Dissolution/

Chemical DissolutionModified Sluicing High-Pressure

Water

C-106*• Capacity of tank: 530 Kgals

• Volume removed: 189 Kgals

• *TPA Appendix H exemption

request pending

C-103• Capacity of tank: 530 Kgals

• Completion date: Aug. 26,

2006

• Volume removed: 75 Kgals

C-104• Capacity of tank: 530 Kgals

• Completion date: Aug. 17, 2012

• Volume removed: 257.3 Kgals

C-107• Capacity of tank: 530 Kgals

• Completion date: Aug. 9, 2014

• Volume removed: 210.4 Kgals

C-203• Capacity of tank: 55 Kgals

• Completion date: March 24, 2005

• Volume removed: 2,501 gallons

C-204• Capacity of tank: 55 Kgals

• Completion date: Dec. 11,

2006

• Volume removed: 1,349

gallons

C-109• Capacity of tank: 530 Kgals

• Completion date: Sept. 13,2012

• Volume removed: 62.2 Kgals

C-112• Capacity of tank: 530 Kgals

• Completion date: Apr 18, 2012

• Volume removed: 91.3 Kgals

C-201• Capacity of tank: 55 Kgals

• Completion date: March 23, 2006

• Volume removed: 718 gallons

C-108• Capacity of tank: 530 Kgals

• Completion date: March 22, 2012

• Volume removed: 63.0 Kgals

C-101• Capacity of tank: 530 Kgals

• Completion date: Sept. 12,2013

• Volume removed: 72.5 Kgals

C-111• Capacity of tank: 530 Kgals

• Completion date: March 20, 2016

• Volume removed: 27.6 Kgals

C-202• Capacity of tank: 55 Kgals

• Completion date: Aug. 11, 2005

• Volume removed: 1,253 gallons

S-112• Capacity of tank: 758 Kgals

• Completion date: March 2, 2007

• Volume removed: 612 Kgals

C-110• Capacity of tank: 530 Kgals

• Completion date: Oct. 15,

2013

• Volume removed: 176.3 Kgals

C-102• Capacity of tank: 530 Kgals

• Completion date: Apr. 9, 2015

• Volume removed: 300.5 Kgals

AY-102• Capacity of tank: 1,000 Kgals

• Volume of waste to be removed: 744 Kgals

• Retrieval began March 2016

• Volume of waste removed: 725 Kgals

C-105 • Capacity of tank: 530 Kgals

• Volume of waste to be removed: 30.4 Kgals

• Retrieval began June 2014

• Volume of waste removed to date: 54.9 Kgals

AX-101 / AX-102 / AX-103 / AX-104

Updated June 2017

8

C-105 Retrieval

• Single-shell tank C-105 is the last

of 16 tanks to be retrieved in C

Farm. Approximately 30,000

gallons of waste remain in the tank.

• Installation of two extended-reach

sluicers is nearly complete. The

sluicers will be used to help

retrieve the remaining waste.

• The final round of retrieval is

expected to begin in August and be

completed in late 2017 or early

2018.

Crews check whether a riser will allow for the

installation of new equipment needed to

complete retrieval.

9

A-AX Single-Shell Tank Farms

• Cleaned out eight pits to support long-

length equipment removal from tanks

AX-102 and AX-104 – the first to be

retrieved.

• Cleanout included removal of old

jumpers, leak detectors and

miscellaneous components.

• Removed first piece of long-length

equipment (thermocouple from AX-102).

• Field testing AX exhausters and

ventilating AX Farm tanks.

• Continued fabrication of two exhausters

to be used to ventilate A Farm tanks

during equipment removal/installation

and retrieval activities.The thermocouple is placed in a grout

box and will be shipped to ERDF for

permanent disposal.

10

Single-Shell Tank T-111

Tank T-111 Pool on June 2, 2015

Tank T-111 Pool on November 16, 2016

Edge of pool

at start of

exhauster

operation

• T-111 exhauster

operated for 7,382 hours

between July 2015 and

December 2016.

• Estimated 7,150 gal of

water removed (~6,400

from sludge; ~750 from

pool)

• Volume of water

evaporated is equivalent

to over 10 years’ worth

of leakage at estimated

2014 leak rate

(~1.8 gal/day).

11

242-A Evaporator Campaign

• First of two planned Evaporator

campaigns this summer was

completed July 15.

• 16-day campaign created about

200,000 gallons of double-shell

tank space.

• Comprehensive industrial

hygiene control strategy was

implemented for the campaign

to monitor and evaluate data

and brief workers.

• The next campaign is set to

begin in mid- to late August and

is expected to create an

additional 280,000 gallons of

tank space.

12

Liquid Effluent Retention Facility

• Installation of a new fabric cover

on one of the three large Liquid

Effluent Retention Facility’s

(LERF) storage basins is nearly

complete.

• First replacement of LERF basin

cover since operations began at

facility in 1994.

• Replacement of second basin

cover planned for FY 2018.

• LERF stores wastewater

generated by 242-A Evaporator

campaigns.

• Each of the LERF basins is

permitted to hold ~7.8 million

gallons of material.

Basin 43

Effluent Treatment Facility

13

Double-Shell Tank AZ-101

Suspect Area

December 2016

Suspect area following the crawler moving

along the annulus floor. (Note crawler tracks)

Current view of

suspect area

Anomaly visible on Bellows

Anomaly is almost directly above the spot observed in

the annulus

14

Double-Shell Tank AY-102

• ~98% of waste removed

(over 744,000 total gallons)

• ~19,000 gal remaining as

of February 2017 (limit of

technologies)

• Standard and extended

reach sluicing systems

used to retrieve waste

• Inspection with high-

definition video camera

conducted in June 2017

• Video inspections will help

inform decision to repair or

close tank per settlement

agreement with State of

Washington

AY-102

6/19/2017

15

Video: AY-102 Inspection

16

Chemical Vapors Management

• Work to extend the 242-A

Evaporator stack from 63 feet

to 111 feet above ground was

completed in mid-June prior to

the start of the Evaporator

campaign.

• Down-select of detection and

monitoring technologies is

underway.

• Air-purifying respirator filter

cartridge testing continues.

• Visit www.HanfordVapors.com

for more information.

17

Phased Implementation Plan (IP)

Additional Recommendations from

Workforce and External Assessments

Hanford Vapors Integrated Safety Management Strategy

Comprehensive Vapor Action Plan (CVAP)

Tank Vapor Assessment Team (TVAT) Recommendations

Integrated Vapors Management Strategy

18

Waste Treatment &Immobilization Plant

1919

Pretreatment

Facility

Analytical

Laboratory

Low-Activity

Waste Facility

High-Level

Waste Facility

Balance of Facilities(20 support buildings)

Waste Treatment andImmobilization Plant (WTP)

Future Site of

LAWPS Facility

Building 87

Effluent Management

Facility Site

20

DFLAW Facility Overview

21

The assembly of Melter No. 1 for the LAW Facility was

completed in June. Construction crews are now focused on

safely assembling the second LAW melter.

Assembly of

300-ton melter

complete

Video:

Low-Activity Waste Facility

22

WTP Analytical Laboratory

• Facility will provide processing information on WTP feed to ensure efficient WTP operations

• Analyses will be performed to meet permitting, process control, authorization basis, and waste form

qualification requirements

• The Lab is designed for continuous operation to support peak throughput for the WTP

• Proposed Lab Operating Permit available for public comment through September 1

23

More Progress at WTP

Three autosamplers were received at the

High-Level Waste Facility. When the plant

is operational, the autosampling system

will ensure the glass produced by the Vit

Plant meets all regulatory standards and

requirements.

The Balance of Facilities switchgear building, also known

as Building 91, was energized in March.

24

Low-Activity Waste Pretreatment System

• Completed 60% Design Review.

• Completed Preliminary Safety

Design Report.

• Developing system testing

reports.

• Permit modification available for

public comment through Sept.

15, 2017; public meeting Aug. 21

at Richland Library.

• Requesting DOE HQ approval of

Critical Decision 3A to begin site

preparation and fabrication of

selected equipment.

• Anticipating full construction

start by mid-FY 2019.

25

Pretreatment Facility Technical Issues Resolution

➢ Multiple technical challenges associated with ventilation system, including high-efficiency particulate air (HEPA) filters

➢ Complete engineering/nuclear safety assessments to ensure ventilation meets requirements

➢ Seismic ground motion criteria for WTP changed around 2005

➢ Complete structural analysis of standard vessel and strategy for structural upgrades to installed vessels

➢ Perform failure modes, effects, and criticality analysis➢ Complete conceptual design of planning areas 2, 3, and 4

➢ Concern with adequacy of pulse jet mixer (PJM ) mixing and control system

➢ Complete testing of standard high solids vessel prototype

➢ Uncertainties exist in waste feed characteristics and ability to meet 40-year service life

➢ Confirm erosion/corrosion design basis, including margin, through testing and analysis

➢ Flammable gases generated by waste treated in WTP could accumulate in process piping and cause deflagration event

➢ Resolved by updating WTP safety basis, basis of design, and process piping design criteria to prevent or control potential

hydrogen explosions

➢ Dense fissile particles could settle on the bottom of Waste Treatment and Immobilization Plant (WTP) vessels with sufficient

mass and geometry such that a criticality event is credible

➢ Issue resolved via calculations, engineering and chemistry studies, criticality safety evaluations, and integrated process

controls

➢ Risk of combustion in the headspace of high-solids vessels due to hydrogen accumulation

➢ Resolved with approval of revised hydrogen safety control strategy consisting of both preventive and mitigative safety and

process controls

Resolved* Testing underway Ongoing

T1 Hydrogen Gas Events in

Vessels*

T2 Criticality in Pulse-Jet Mixer

(PJM) Vessels*

T3 Hydrogen in Piping and

Ancillary Vessels*

T4 PJM Vessel Mixing and

Control

T5 Erosion/Corrosion in Piping

and Vessels

T6 Design Redundancy/In Service Inspection

T7 Black Cell Vessel/ Equipment

Structural Integrity

T8 Facility Ventilation/Process

Off-Gas Treatment

*This technical issue has been sufficiently resolved to allow engineering to

proceed in support of design and safety basis development.

26

➢ ORP striving to have all remaining technical

issues resolved in 2018 and return WTP

Pretreatment to design

➢ WTP Pretreatment production engineering to

proceed following technical issue resolution

and availability of project funding

➢ Complete facility designs and safety basis

documentation in accordance with federal

regulations

Technical Issues Resolution Path Forward

27

STEM Outreach

“The students’ interaction with you

helped them grow and mature

tremendously. This is unquestionably

among the most important elements in

their education and development in

becoming practicing engineers.”

- Marc Levin, Professor of Energy

Production at Voiland School of Chemical

Engineering and Bioengineering,

WSU Pullman

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“Protecting our workers, the public, and the environment”