Eo-...RPP-RPT-42744, Rev.0 1 2009 Auto-TCR for Tank 241-A-106 _____ Some of the reports herein may...

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(1) Document Number: RPP-RPT-42744 (2) Revision Number: 0 (3) Effective Date: 9/15/2009

(4) Document Type: ElDigital Image ElHard copy (a) Number of pages (including the DRF) or 7'~ PO ~ Vdeonumber of digital images

(5) Release Type N New El Cancel L: Page Change l Complete Revision

(6) Document Title: 2009 Auto-TCR for Tank 241 -A-i 06

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(8) Change Initial IssuanceJustification:

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Documents: ___________________I____________________

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R.S. Disselkamp 9/15/2009(b) Responsible Manager (Printl gnfr Date:

J.G. Reynolds J2:14 77 ' 9/15/2009(c) Reviewer (Optic I, Print/Sign): JDate:

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(14) Date:

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A-6003-881 (REV 1)

RPP-RPT-42 744, Rev. 0

2009 Auto-TCR for Tank 241 -A-I 06

R.S. DisselkampWashington River Protection Solutions LLCRichland, WA 99352U.S. Department of Energy Contract DE-AC27-O8RV1 4800

EDT/ECN: DRF UC: N/ACost Center: 2GBOO Charge Code: -B&R Code: N/A Total Pages: q 1--

Key Words: 241-A-106 tank, Auto-ICR, Tank Inventory Report, Best Basis Inventory

Abstract: The purpose of this report is to publish the AUTO-Tank Characterization Report (AutoTCR)that was automatically generated by the TWINS database. The archiving and retrieval of tank informationwill be performed using a tank-by-tank full document issuance system in the future. This is necessarybecause the software that generates the AutoTCR is no longer compatible with modem hardware operatingsystem(s), and/or interfacing software packages. The purpose of issuing the AutoTCR document is toprovide a snapshot of the inventories and to preserve a historical record of tank data. The text descriptionfor the TCR has not been updated since 2005, with the exception of the Best Basis Inventory. The textcontains tank historical data, procedures used in sample analysis, waste transfer history, and physical andchemical data. The information here was that available in the AutoTCR as of August 2009.

TRADEMARK DISCLAIMER. Reference herein to any specific commercial product, process, or service by trade name,trademark, manufacturer, or otherwvise, does not necessarily constitute or imply its endorsement, recommendation, orfavoring by the United States Government or any agency thereof or its contractors or subcontractors.

SEiP 1 20DATE: HANFORD

STA:Ji RELEASE '0D

Release Approval Date Release Stamp

Approved For Public Release

A-6002-767 (REV 2)

RPP-RPT-42744, Rev.0

1

2009 Auto-TCR for Tank 241-A-106

_____________________________________________________________________________

Some of the reports herein may contain data that has not been reviewed or edited. The

data will have been reviewed or edited as of the date that a Tank Interpretive Report

(TIR) is prepared and approved. This tank has no TIR, use the data with this caution in

mind.

Tank: 241-A-106

Sampling Events:

Reports:

Analytical Methods and Procedures

Best Basis Inventory Without Details

Best Basis Inventory Without Details Supplementals

Core Profiles

Data Source Reference List

Description of Tank

Dilution and Mixing Studies

Major Transfers

Means and Confidence Intervals

Rheology Report

Riser Configuration for Tank

Sample Breakdown Diagrams

Standard Acronym Definitions

Tank Interpretive Report

Tank Subsampling Scheme and Sample Description

Tank Surface Level

Tank Temperature Profile

Constituent Groups:

Anions

Inorganics

Metals/Nonmetals

Organics

PCBs

Physical Properties

Radionuclides


2

Table of Contents

Data Dictionary to Reports in this Document ................................................................................. 3

Tank Interpretive Report For 241-A-106 ...................................................................................... 10

Description of Tank 241-A-106 .................................................................................................. 155

Riser Configuration for Tank 241-A-1061,2,3,4,5,6

........................................................................ 166

Tank 241-A-106 Best Basis Inventory Without Details ............................................................. 177

Tank 241-A-106 Best Basis Inventory Without Details -- Supplementals ................................. 355

Tank 241-A-106 Analytical Methods and Procedures.................................................................. 40

Tank 241-A-106 Subsampling Scheme and Sample Description ................................................. 41

241-A-106 Sample Breakdown Diagrams .................................................................................... 42

241-A-106 Rheology Report......................................................................................................... 43

241-A-106 Means and Confidence Intervals .............................................................................. 434

Solid Data................................................................................................................................ 434

241-A-106 Means and Confidence Intervals .............................................................................. 445

Liquid Data ............................................................................................................................. 445

Tank 241-A-106 Transfers (1994 to present) ............................................................................. 456

241-A-106 HTCE Surface Levels ............................................................................................... 467

241-A-106 Average Monthly Tank Surface Level (after 1/1/96 only) ....................................... 478

241-A-106 Tank Temperature Profile ........................................................................................ 489

241-A-106 Core Profiles ............................................................................................................... 50

Tank 241-A-106 Data Source Reference List ............................................................................... 51

Tank 241-A-106 Dilution and Mixing Studies ........................................................................... 687

Standard Acronym Definitions ................................................................................................... 698


3

Data Dictionary to Reports in this Document

Report Field Description

Tank Interpretive Report Interprets information about the tank

answering a series of standard questions

covering areas such as information drivers,

tank history, tank comparisons, disposal

implications, data quality and quantity, and

unique aspects of the tank.

Description of Tank Provides an executive summary of

information about the tank including tank

description, tank status, sampling dates, and

service status.

Tank Description Section provides basic physical information

for the tank.

Type Single or Double Shell Tank

Constructed Year(s) the tank was constructed

In-Service Month/Year the tank was put into service

Diameter Distance across the tank (in meters and feet)

Operating Depth Depth of allowable operation (referenced to

the tank bottom) (in centimeters and feet)

Design Capacity Tank waste volume if filled to its operating

capacity (in kiloliters and kilogallons)

Bottom Shape Shape of the tank bottom (flat or dish)

Ventilation Type of ventilation system on the tank (active

or passive)

Tank Status (as of date) Section provides current status information

for the tank. Date reported is the effective

date of the most recent BBI effective date


4



Volumes:

Total Waste Volume

Supernatant Volume

Retained Gas Volume

Ret Gas Sludge Volume

Ret Gas Saltcake

Volume

Saltcake Liquid Volume

Saltcake Solid Volume

Sludge Volume

Tank vols from the most recent Best Basis

Inventory (BBI) update. All BBI waste

phases are listed, but the vol is left as NA if

the BBI does not have an estimate for that

phase. For example, tank AN-103 does not

contain sludge, so the Sludge vol is reported

as NA. In most DSTs, the saltcake liquid

and saltcake solids are combined into a single

total saltcake phase. These are reported

under the saltcake solids category and the

liquid vol is left blank, though liquid does

exist in the tank. Retained gas vols are only

reported if retained gas measurements were

taken. It may be reported as associated with

a particular phase (saltcake or sludge), or

simply as the retained gas vol. All vols are

listed in kL and kgal.

Surface Level (date) Surface level provided in PCSACS that

corresponds to the BBI volume effective date

(effective date shown). Provided in

centimeters and inches.

PCSACS Surface Level

(date)

Most recent surface level provided in the

PCSACS database (effective date shown).

Provided in centimeters and inches.

Temperature (date range) Minimum and maximum temperature of tank

over the one year range preceding BBI

volume effective date (range shown). Data is

from the PCSACS database. Data is

provided in degrees Celsius and Fahrenheit.

Temperature (date) Minimum and maximum temperature of tank

(all thermocouples) of the most recent

readings (date specified). Data is from

PCSACS database. Data is provided in

degrees Celsius and Fahrenheit.

Integrity Sound, assumed leaker, or known leaker.

Based on Waste Tank Summary Report

(HNF-EP-0182, latest Rev)

Flammable Gas Facility

Group

Waste group category as defined in RPP-

10006. May be category A, B, or C.


5



Sampling Dates:

Core Samples

Grab Samples

Vapor Samples

Auger Samples

The dates when sampling was performed on

this tank as provided in the TWINS Tank

Characterization Database, and Tank Vapor

Database. If none are listed, no sampling has

occurred in the tank since approximately

1992.

Service Status Section provides dates of common points of

interest in the tank’s history. Date is left

blank or NA if the subject is not applicable.

Declared Inactive Date the tank was declared inactive.

Interim Stabilization Date interim stabilization was completed.

Intrusion Prevention Date intrusion prevention was completed.

Riser Configuration for Tank Shows riser numbers, diameters, and a

description of the risers.

Best Basis Inventory Without Details Contains best basis inventory without details

for the contents of the Hanford waste tanks.

Analyte The name of the constituent used for

reporting purposes.

Waste Phase Waste Phase is the phase of waste to which

the concentration data is applicable (e.g.,

supernatant, saltcake, sludge, liquid, solid,

etc.).

Waste Type Waste Type is the waste type as defined in

HDW Rev. 4 or as defined by "templates"

(e.g. , SMMA1, SMMT1, etc.).

Volume Volume of the waste phase

Concentration Concentration reported in uCi/g, ug/g,

uCi/mL, or ug/mL

Inventory Best Basis Inventory estimate, reported in kg

or Ci

Basis The basis for the inventory value.

Comment Further information to clarify the information

in the table.

Best Basis Inventory Without Details

Supplementals

Contains best basis inventory without details

for the contents of the Hanford waste tanks

for the supplemental analytes not part of the

BBI.


reporting purposes.


6



Waste Phase Waste Phase is the phase of waste to which

the concentration data is applicable (e.g.,

supernatant, saltcake, sludge, liquid, solid,

etc.).

Waste Type Waste Type is the waste type as defined in

HDW Rev. 4 or as defined by "templates"

(e.g. , SMMA1, SMMT1, etc.).

Volume Volume of the waste phase

Concentration Concentration reported in uCi/g, ug/g,

uCi/mL, or ug/mL

Inventory Best Basis Inventory estimate, reported in kg

or Ci

Basis The basis for the inventory value.

Comment Further information to clarify the information

in the table.

Analytical Methods and Procedures Lists procedure numbers and applicable

analyses. Optionally displays appropriate

analytes for each analyses.


reporting purposes.

Method Name assigned to the general group of

laboratory analytical methods to which the

current method belongs.

Procedure Laboratory procedure identifier.

Tank Subsampling Scheme and Sample

Description

Contains information on samples taken in a

sampling event including sample

identification, sample weight, percent of

sample recovery and sample physical

appearance.

Sample Location Riser and surface level

Sample Event Identification number of a sampling event

collected from a waste site. For cores, a core

number, for supernate samples, a supernate

sample number, and for surface samples, a

surface sample number is provided.

Amount Mass of the sample in grams and/or volume

of the sample in milliliters

Aggregation Level Description of the portion of the original tank

sample represented by the current sample.


7



Sample Characteristics Description of the physical appearance of the

sample.

Sample Breakdown Diagrams Sample Breakdown Diagrams show the

pedigree for each of the sample vials drawn

from a tank waste material source, such as

core sample, auger sample, or grab sample.

Rheology Report Contains narrative, tables, and graphical

displays of rheological data for this tank.

Analytical Results: Rheology Contains results (primary/ duplicate/

triplicate/ average) of laboratory

measurement of rheological properties of

waste site samples. Grouped by analyte and

procedure.

Sample Number Internal lab identifier assigned by the lab that

analyzed the sample.

Sample Location Location from which sample was taken.

Could be core and segment or riser

identification depending on the sampling

type.

Sample Portion Description of the portion of the original tank


Result Primary result of the analysis of the sample.

Duplicate Duplicate result of the analysis of the sample.

Triplicate Triplicate result of the analysis of the sample.

Average Average of the primary, duplicate, and

triplicate results.

Sample Attributes Contains list of sample attributes for altered

samples included in the report.



Attribute Name Name of the sample attribute.

Attribute Value and units or textual description of the

sample attribute.

Rheology Measurements Contains graphical displays of rheology data

for this tank.




8



Sample Location Location from which sample was taken.

Could be core and segment or riser

identification depending on the sampling

type.

Sample Portion Description of the portion of the original tank


Result Type Association of displayed data with a result

(primary), duplicate, or triplicate

measurement.

Project Type Internal identifier assigned in order to specify

that the reported measurement was made on

an unaltered tank sample (Unaltered), an

altered tank sample (Altered), or a baseline

sample in a project requiring sample

alteration (Semi-Altered).

Means and Confidence Intervals Contains statistical analysis data for tank

content including means and variances.


reporting purposes.

Method Name assigned to the general group of

laboratory analytical methods to which the

current method belongs.

Mean Average of the primary, duplicate, and

triplicate results.

df Degrees of freedom

LL Lower 95% limit

UL Upper 95% limit

Units Measurement units

Major Transfers Waste Transfers summarizes the waste

transfer history of the tank after January 1,

1994.

Transfer Source The description of the source of the waste

that was transferred.

Transfer Destination The description of the destination of the

waste that wast transferred.

Waste Type The description of the type of waste that was

transferred.

Time Period The time over which the waste transfer

occurred.


9



Estimated Waste Volume

(kL)

The estimated volume of waste transferred in

kL.

Estimated Waste Volume

(kgal)

The estimated volume of waste transferred in

kgal.

HTCE Surface Level Surface level information as reported in the

1996 Historical Tank Contents Estimate

(HTCE) report.

Tank Surface Level Contains history of current tank waste

surface level plot by year and month.

Tank Temperature Profile Contains history of and current tank

maximum temperature by year and month.

Please note that tank temperature is not

necessarily the same as waste temperature.

Core Profiles Core Profiles are graphical depictions of

physical properties of each segment of a core

of tank waste.

Data Source Reference List Lists the documents found in the Data Source

Access (DSA) database which are appropriate

for this tank. Provides hyperlinks to both the

DSA metadata and to the electronic

documents themselves.

Dilution and Mixing Studies Lists the Dilution and Mixing Studies

documents found in the Data Source Access

(DSA) database which are appropriate for

this tank. Provides hyperlinks to both the

DSA metadata and to the electronic

documents themselves.

Standard Acronym Definitions Contains acronyms and abbreviations with

definitions

Acronym Acronym or abbreviation

Definition Definition of an acronym or abbreviation


10

Tank Interpretive Report For 241-A-106

Best-Basis Inventory Derivation Text: Tank 241-A-106

The Best-Basis Inventory (BBI) effort involves developing and maintaining waste tank

inventories comprising 25 chemical and 46 radionuclide components in the 177 Hanford Site

underground storage tanks. These BBIs provide waste composition data necessary as part of the

River Protection Project (RPP) process flowsheet modeling work, safety analyses, risk

assessments, and system design for waste retrieval, treatment, and disposal operations.

Development and maintenance of the BBI is an on-going effort. A liquid observation well

(LOW) was installed in tank 241-A-106 in August 2002. A review of the LOW data indicates

that the tank contains more interstitial liquid than previously predicted. As a result, a re-

evaluation of the BBI for tank 241-A-106 as of October 1, 2005 was performed and is

documented in the following text. The following information was used in this evaluation:

Average concentrations from a 1986 push-mode core sampling event (WHC-SD-RE-TI-200,

Data Transmittal Package for 241-A-106 Waste Tank Characterization).

Average concentrations from a 1996 tank 241-A-102 auger sampling event, auger

96-AUG-003 (WHC-SD-WM-DP-177, Final Report for Tank 241-A-102, Auger Sample 96-

AUG-003, and HNF-SD-WM-ER-721, Preliminary Tank Characterization Report for Single-

Shell Tank 241-A-106: Best-Basis Inventory).

BBI templates for 242-A evaporator saltcake (A1-SltCk), strontium recovery waste (SRR),

and washed PUREX HLW sludge (AR) (RPP-8847, Best-Basis Inventory Template

Compositions of Common Tank Waste Layers). The waste type templates are based on

sample data for similar tank wastes supplemented with HDW model data (RPP-19822,

Hanford Defined Waste Model – Revision 5) where sample data are not available.

Process knowledge estimates for total polychlorinated biphenyls (PCB) in each waste phase

(RPP-7625, Best-Basis Inventory Process Requirements).

Table 8-1 summarizes how the best-basis inventories for tank 241-A-106 were derived.


11

Table 8-1. Tank 241-A-106 Best-Basis Inventory Source Data.

Waste

Phase

Waste

Type

Applicable

Concentration Data1

Associated

Density

(g/mL)

Multiplier

Associated

Volume

Salt Cake

(solids)

A1-

SltCk

Average of the 1986

Cores 1 & 2 Sampling

Event (P/A106/001)

1.55 1.391 110 kL

(29 kgal)

Tank A-102 1996 AUG-

003 Sample

(P/A102/005)

1.70 1.081

A1-SltCk Solids Template

(TS/U204/025)

1.58 1.136

A-106 A1-SltCk Solids

PCBs (P/A106/003)

1.70 1.000

Sludge2

SRR

Average of the 1986


Event (P/A106/001)

1.55 1.391 110 kL

(29 kgal)


003 Sample (P/A102/005)

1.70 1.081

SRR Sludge Template

(TE/U204/093)

1.51 1.960

A-106 SRR Sludge PCBs

(P/A106/005)

1.70 1.000

AR

Average of the 1986


Event (P/A106/001)

1.55 1.391 79 kL

(21 kgal)


003 Sample (P/A102/005)

1.70 1.081

AR Solids Template

(TE/U204/048)

1.34 2.653

A-106 AR Solids PCBs

(P/A106/004)

1.70 1.000

Total tank

299 kL

(79 kgal)

Notes: 1Vector handles, shown in parentheses, are unique serial identifiers for the

vectors used in the BBIM database. 2The sludge waste phase includes both solids and interstitial liquid; the

interstitial liquid volume was estimated to be 34 kL (9.0 kgal).

Tank 241-A-106 received and transferred Plutonium-Uranium Extraction (PUREX) process (P)

waste from 1957 through 1973. The tank was sluiced as part of the B-Plant strontium recovery

campaign in the early 1970’s with a final sluicing to tank 241-AY-101 in 1977. Tank 241-A-106

received 242-A Evaporator bottoms saltcake from 1976 through 1978. The tank was labeled

inactive in August 1980. The tank was administratively interim stabilized in August 1982

(HNF-SD-RE-TI-178, Single-Shell Tank Stabilization Record).


12

Tank 241-A-106 auto and manual ENRAF readings on January 1, 2001 were 28.76 inches,

corresponding to 299 kL (79 kgal). Readings taken October 1, 2005 indicate a tank waste level

of 25.14 inches. On June 25, 2002, there was a calibration shift as a result of calibrating and

flushing of the measurement weight assembly. This sudden shift essentially accounted for the

difference in the measurements. The shift in level measurements was likely due to a localized

surface depression caused by the water flush. Therefore, the total waste volume was estimated

based on the January 1, 2001 measurement.

Liquid observation well (LOW) measurement on August 1, 2005 was 19.2 inches. It appeared

from the LOW graph that the reading was a waste surface measurement. The waste volume

based on the LOW measurement is 200 kL (53 kgal). This is approximately the same as the

sludge volume estimated based on revision 4 of the HDW (LA-UR-96-3860, Hanford Tank

Chemical and Radionuclide Inventories: HDW Model Rev. 4). One possible explanation is that

the saltcake at this location was removed during installation of the LOW. Saltcake located above

the sludge and away from the LOW may contain interstitial liquid held in place by capillary

effects. Therefore, the LOW measurement is an indication of the minimum interstitial liquid

level in the tank. For this BBI, it was assumed that only the bottom 19.2 inches of sludge waste

contained interstitial liquid. Assuming an average sludge porosity of 0.17 (HNF-2978, Updated

Pumpable Liquid Volume Estimates and Jet Pump Durations for Interim Stabilization of

Remaining Single-Shell Tanks) is applicable to the sludge in the tank, the volume of interstitial

liquid in the sludge was estimated to be 34 kL (9.0 kgal).

According to LA-UR-96-3860, the chemical inventory of the waste in tank 241-A-102 closely

resembles the waste in tank 241-A-106. Both tanks 241-A-102 and 241-A-106 contain SRR and

A1-SltCk waste; however, according to LA-UR-96-3860, AR waste is not in the listing for tank

241-A-102. Because the major portion of tank 241-A-106 waste was transferred back to tank

241-A-102, and due to the extensive interaction and similarity of process history, tank

241-A-102 is considered a reasonable candidate to predict some of tank 241-A-106 analytes not

provided in the 1986 sampling event (HNF-SD-WM-ER-721).

Since the tank 241-A-106 analyte inventory has not changed since the core sample was taken in

1986, the data is considered to be the best approximation of the tank inventory at this time. The

data for the two core analyses of tank 241-A-106 (WHC-SD-RE-TI-200) were averaged to

develop the process-based inventory concentration (P/A106/001). Based on surface level

measurements taken in 1987 and 1988, it was estimated that tank 241-A-106 contained

approximately 416 kL (110 kgal) at the time it was sampled. A multiplier of 1.391 (416 kL / 299

kL = 1.391) was applied to account for the loss of water due to evaporation since sampling in

1986. LA-UR-96-3860 indicates that approximately 189 kL (50 kgal) of the waste matrix was

sludge (partitioned to represent the SRR and AR estimated portion of the sludge matrix) and the

remainder was saltcake. The sludge volumes listed in Table 8-1 are based on revision 4 of the

HDW (LA-UR-96-3860), and the remaining volume is assumed to be saltcake.

The densities used in the best-basis inventory calculations were either the analytically

determined value from the 1986 sample (1.55 g/mL), the A-102 sample means (1.70 g/mL), or

the BBI template densities. The measured weight percent water were 44% and 34.3% for the

1986 core composite and the A-102 auger samples (respectively). The 1986 sample density and

wt% water were not documented to current quality control requirements nor is the analysis as

comprehensive as is now done for current samples. A multiplier of 0.777 was calculated for the


13

241-A-102 data based on the above densities and wt% water. The final multiplier for the tank

241-A-102 data is 1.081 after the 1.391 waste concentration factor is included.

Multipliers were also developed for the waste type templates. Templates are based on sampling

data from tanks that contain the same waste type as tank 241-A-106, supplemented with revision

5 HDW model data (RPP-19822). A multiplier is used to scale the template vector to the sample

data using the sample weight percent water and density. A more detailed description of these

multipliers is found in RPP-8847. Since the waste volume has been significantly reduced by

water evaporation since the 1986 sampling event, the component density and weight percent

water were selected from the tank 241-A-102 data (1.7 g/mL and 34.3 wt%) as this better

represents the current 241-A-106 waste condition. The multipliers for the A1-SltCk, SRR sludge

and AR sludge template data are 1.136, 1.960 and 2.653 respectively.

The inventories in this BBI were developed in accordance with the BBI rules in RPP-7625. All

inventory calculations were performed using the Best-Basis Inventory Maintenance (BBIM)

Tool. The updated BBI values for tank 241-A-106 are shown in the Best-Basis Inventory

Without Details standard report. Radionuclides in the Best-Basis Inventory Without Details

standard report are decay-corrected to January 1, 2008.

Alpha-emitting isotopes: Data from analysis of 239/240

Pu, 241

Am, and total uranium and the

template isotopic distribution ratios were used to generate inventories for the various alpha-

emitting isotopes.

PCBs: A total PCB inventory is estimated per guidelines established in RPP-7625. A default

PCB concentration of 25 µg/g (wet weight) was used for solids since current sample data were

not available.

Changes Since Previous BBI: Liquid observation well (LOW) data were used to update the

estimate of interstitial liquid volume. Constituent inventories were not affected.


14

REFERENCES

HNF-2978, 2003, Updated Pumpable Liquid Volume Estimates and Jet Pump Durations for

Interim Stabilization of Remaining Single-Shell Tanks, Rev. 5, CH2M HILL Hanford

Group, Inc., Richland, Washington.

HNF-SD-RE-TI-178, 2001, Single-Shell Tank Stabilization Record, Rev. 7, CH2M HILL

Hanford Group, Inc., Richland, Washington.

HNF-SD-WM-ER-721, 1998, Preliminary Tank Characterization Report for Single-Shell Tank

241-A-106: Best-Basis Inventory, Rev. 0A, COGEMA Engineering Corporation,

Richland, Washington.

LA-UR-96-3860, 1997, Hanford Tank Chemical and Radionuclide Inventories: HDW Model

Rev. 4, Los Alamos National Laboratory, Los Alamos, New Mexico.

RPP-7625, 2004, Best-Basis Inventory Process Requirements, Rev. 5, CH2M HILL Hanford


RPP-8847, 2004, Best-Basis Inventory Template Compositions of Common Tank Waste Layers,

Rev. 1, CH2M HILL Hanford Group, Inc., Richland, Washington.

RPP-19822, 2004, Hanford Defined Waste Model – Revision 5, Rev. 0, CH2M HILL Hanford


WHC-SD-RE-TI-200, 2004, Data Transmittal Package for 241-A-106 Waste Tank

Characterization, Rev. 0A, CH2M HILL Hanford Group, Inc., Richland, Washington.

WHC-SD-WM-DP-177, 1998, Final Report for Tank 241-A-102, Auger Sample 96-AUG-003,

Rev. 1A, Waste Management of Hanford, Inc., Richland, Washington.


15

Description of Tank 241-A-106

TANK DESCRIPTION

Type Single Shell

Constructed 1954-1955

In-service 3/1957

Diameter 22.9 m (75 ft)

Operating Depth 914.4 cm (360 in)

Design Capacity 3785 kL (1000 kgal)

Bottom shape flat

Ventilation Operating Exhauster

TANK STATUS (as of 10/1/2004)

Total Waste Volume 299 kL (79 kgal)

Supernatant Volume NA

Retained Gas Volume NA

Retained Gas - Sludge Volume NA

Retained Gas - Salt Cake Volume NA

Salt Cake Liquid Volume NA

Salt Cake Solid Volume 110 kL (29 kgal)

Sludge Volume 189 kL (50 kgal)

Surface Level (10/1/2004) 63.7 cm (25.1 inches)

PCSACS Surface Level (11/13/2005) 63.9 cm (25.2 inches)

Temperature (10/1/2003 - 9/30/2004) None

Temperature (6/3/2005) 52.9oC - 52.9

oC (127.2

oF - 127.2

oF)

Integrity Sound

Waste Group Designation C

SAMPLING DATES (See Note Below)

Vapor Samples 1/16/1997

SERVICE STATUS

Declared Inactive 1980

Interim Stabilization August 1982

Intrusion Prevention December 1982

Note: the date(s) shown here are taken from the sample chain of custody documents. The

date(s) may be different than the dates indicated on the Core Profile standard report.


16

Riser Configuration for Tank 241-A-1061,2,3,4,5,6

Number Diameter

(Inches)

Description and comments

1 8 Drywell, [BM CEO36404 12/11/86]

2* 8 Welded Flange

3 12 Air Circulator Lines, Cut and Capped

4 12 Pit 06D Riser, WC

5 4 Crust Breaker, WC

6 4 FIC, [BM CEO36404 12/11/86]

7* 4 Blind Flange (Lead Cap)

8 4 Pit 06D Drain, WC

9 20 Vapor Riser, BG

10* 6 SMP

11* 6 SMP, [BM CEO36404 12/11/86]

12* 6 SMP, Blind Flange

14 4 Temperature

15 8 WT Factor Dip Tube, WC [Remove ECN171167, 5/12/92]

16 42 Pump, WC

17* 12 Flange/B-222 Observation Port

18* 4 Breather Filter

20* 6 Blind Flange

21 12 Sluice Pit 06B Pump, WC

22 12 Sluice Pit 06C Pump, WC

N1 6 Overflow Inlet

N2 3 Entrainment Tank Drain, Capped BG

N3 3 Fill Line V068, Sealed in Valve Pit 241-A-501

N4 3 Fill Line V048, Sealed in Diversion Box 241-A-152

N5 3 Spare Line V049, Sealed in Diversion Box 241-A-152

Notes: 1Tran (1993)

4H-2-73394, Rev. 2

2Alstad (1993)

5H-2-66030, Rev. 2

3Lipnicki (1996)

6H-2-55910, Rev. 6

* Denotes risers tentatively availalbe for sampling (Lipnicki 1996)


17

Tank 241-A-106 Best Basis Inventory Without Details

Decayed To: January 1, 2008

Effective Date: October 1, 2005

Published On: February 29, 2008

Best Basis Derivation

Analyte Waste Phase Waste Type Volume Concentration Inventory Basis Comment

Al Saltcake Solid A1-SltCk (Solid) 110 kL 3.16E+ 04 g/g 5.40E+ 03 kg E

Al Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 3.16E+ 04 g/g 5.40E+ 03 kg E

Al Sludge (Liquid

& Solid)

AR (Solid) 79 kL 3.16E+ 04 g/g 3.87E+ 03 kg E

Al Total 299 kL 1.47E+ 04 kg

Bi Saltcake Solid A1-SltCk (Solid) 110 kL 2.55E+ 02 g/g 4.34E+ 01 kg E

Bi Sludge (Liquid

& Solid)


Bi Sludge (Liquid

& Solid)


Bi Total 299 kL 1.18E+ 02 kg

Ca Saltcake Solid A1-SltCk (Solid) 110 kL 7.33E+ 03 g/g 1.25E+ 03 kg E

Ca Sludge (Liquid

& Solid)


Ca Sludge (Liquid

& Solid)


Ca Total 299 kL 3.40E+ 03 kg

Cl Saltcake Solid A1-SltCk (Solid) 110 kL 8.62E+ 03 g/g 1.61E+ 03 kg E

http://twinswhse.pnl.gov/tcr.nsf/d96c5d01e8ba69e08825647b0070bd5a/17F1DA91716ADFE788256B0A0055B795/$FILE/Tank%20A-106%20TIR8%20FY06%20Q1%20-%20Final%20Rev%201.doc


18


Cl Sludge (Liquid

& Solid)


Cl Sludge (Liquid

& Solid)


Cl Total 299 kL 4.38E+ 03 kg .

TIC as

CO3

Saltcake Solid A1-SltCk (Solid) 110 kL 2.34E+ 04 g/g 4.38E+ 03 kg E

TIC as

CO3

Sludge (Liquid

& Solid)


TIC as

CO3

Sludge (Liquid

& Solid)


TIC as

CO3

Total 299 kL 1.19E+ 04 kg .

Cr Saltcake Solid A1-SltCk (Solid) 110 kL 7.05E+ 03 g/g 1.20E+ 03 kg E

Cr Sludge (Liquid

& Solid)


Cr Sludge (Liquid

& Solid)


Cr Total 299 kL 3.27E+ 03 kg

F Saltcake Solid A1-SltCk (Solid) 110 kL 2.99E+ 02 g/g 5.60E+ 01 kg E

F Sludge (Liquid

& Solid)


F Sludge (Liquid

& Solid)


F Total 299 kL 5.74E+ 01 kg Upper bounding

estimate

Fe Saltcake Solid A1-SltCk (Solid) 110 kL 3.67E+ 04 g/g 6.25E+ 03 kg E


19


Fe Sludge (Liquid

& Solid)


Fe Sludge (Liquid

& Solid)


Fe Total 299 kL 1.70E+ 04 kg

Hg Saltcake Solid A1-SltCk (Solid) 110 kL 1.04E+ 00 g/g 1.81E-1 kg E

Hg Sludge (Liquid

& Solid)


Hg Sludge (Liquid

& Solid)


Hg Total 299 kL 2.59E+ 02 kg .

K Saltcake Solid A1-SltCk (Solid) 110 kL 3.13E+ 03 g/g 5.34E+ 02 kg E

K Sludge (Liquid

& Solid)


K Sludge (Liquid

& Solid)


K Total 299 kL 1.45E+ 03 kg

La Saltcake Solid A1-SltCk (Solid) 110 kL 1.11E+ 02 g/g 2.08E+ 01 kg E

La Sludge (Liquid

& Solid)


La Sludge (Liquid

& Solid)


La Total 299 kL 5.66E+ 01 kg .

Mn Saltcake Solid A1-SltCk (Solid) 110 kL 1.97E+ 03 g/g 3.35E+ 02 kg E

Mn Sludge (Liquid

& Solid)



20


Mn Sludge (Liquid

& Solid)


Mn Total 299 kL 9.11E+ 02 kg

Na Saltcake Solid A1-SltCk (Solid) 110 kL 1.70E+ 05 g/g 2.89E+ 04 kg E

Na Sludge (Liquid

& Solid)


Na Sludge (Liquid

& Solid)


Na Total 299 kL 7.86E+ 04 kg

Ni Saltcake Solid A1-SltCk (Solid) 110 kL 8.69E+ 02 g/g 1.48E+ 02 kg E

Ni Sludge (Liquid

& Solid)


Ni Sludge (Liquid

& Solid)


Ni Total 299 kL 4.03E+ 02 kg

NO2 Saltcake Solid A1-SltCk (Solid) 110 kL 8.99E+ 04 g/g 1.68E+ 04 kg E

NO2 Sludge (Liquid

& Solid)


NO2 Sludge (Liquid

& Solid)


NO2 Total 299 kL 4.57E+ 04 kg .

NO3 Saltcake Solid A1-SltCk (Solid) 110 kL 1.09E+ 05 g/g 1.85E+ 04 kg E

NO3 Sludge (Liquid

& Solid)


NO3 Sludge (Liquid

& Solid)


NO3 Total 299 kL 5.03E+ 04 kg


21


Oxalate Saltcake Solid A1-SltCk (Solid) 110 kL 1.29E+ 04 g/g 2.41E+ 03 kg E

Oxalate Sludge (Liquid

& Solid)


Oxalate Sludge (Liquid

& Solid)


Oxalate Total 299 kL 6.54E+ 03 kg .

Pb Saltcake Solid A1-SltCk (Solid) 110 kL 1.45E+ 03 g/g 2.47E+ 02 kg E

Pb Sludge (Liquid

& Solid)


Pb Sludge (Liquid

& Solid)


Pb Total 299 kL 6.72E+ 02 kg

PO4 Saltcake Solid A1-SltCk (Solid) 110 kL 7.48E+ 04 g/g 1.28E+ 04 kg E

PO4 Sludge (Liquid

& Solid)


PO4 Sludge (Liquid

& Solid)


PO4 Total 299 kL 3.47E+ 04 kg

Si Saltcake Solid A1-SltCk (Solid) 110 kL 5.34E+ 04 g/g 9.11E+ 03 kg E

Si Sludge (Liquid

& Solid)


Si Sludge (Liquid

& Solid)


Si Total 299 kL 2.48E+ 04 kg

SO4 Saltcake Solid A1-SltCk (Solid) 110 kL 4.84E+ 03 g/g 9.06E+ 02 kg E


22


SO4 Sludge (Liquid

& Solid)


SO4 Sludge (Liquid

& Solid)


SO4 Total 299 kL 2.46E+ 03 kg .

Sr Saltcake Solid A1-SltCk (Solid) 110 kL 7.23E+ 01 g/g 1.23E+ 01 kg E

Sr Sludge (Liquid

& Solid)


Sr Sludge (Liquid

& Solid)


Sr Total 299 kL 3.35E+ 01 kg

TOC Saltcake Solid A1-SltCk (Solid) 110 kL 9.31E+ 03 g/g 1.59E+ 03 kg E

TOC Sludge (Liquid

& Solid)


TOC Sludge (Liquid

& Solid)


TOC Total 299 kL 4.31E+ 03 kg

UTOTAL Saltcake Solid A1-SltCk (Solid) 110 kL 1.12E+ 03 g/g 1.91E+ 02 kg E

UTOTAL Sludge (Liquid

& Solid)


UTOTAL Sludge (Liquid

& Solid)


UTOTAL Total 299 kL 5.18E+ 02 kg

Zr Saltcake Solid A1-SltCk (Solid) 110 kL 1.67E+ 03 g/g 2.86E+ 02 kg E

Zr Sludge (Liquid

& Solid)



23


Zr Sludge (Liquid

& Solid)


Zr Total 299 kL 7.76E+ 02 kg

3H Saltcake Solid A1-SltCk (Solid) 110 kL 1.01E-2 Ci/g 1.76E+ 00 Ci E

3H Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 5.24E-3 Ci/g 8.70E-1 Ci E

3H Sludge (Liquid

& Solid)

AR (Solid) 79 kL 1.16E-2 Ci/g 1.23E+ 00 Ci E

3H Total 299 kL 3.86E+ 00 Ci

14C Saltcake Solid A1-SltCk (Solid) 110 kL 1.12E-3 Ci/g 1.91E-1 Ci E

14C Sludge (Liquid

& Solid)


14C Sludge (Liquid

& Solid)

AR (Solid) 79 kL 1.12E-3 Ci/g 1.37E-1 Ci E

14C Total 299 kL 5.18E-1 Ci

59Ni Saltcake Solid A1-SltCk (Solid) 110 kL 8.67E-3 Ci/g 1.51E+ 00 Ci E

59Ni Sludge (Liquid

& Solid)


59Ni Sludge (Liquid

& Solid)


59Ni Total 299 kL 1.13E+ 01 Ci

60Co Saltcake Solid A1-SltCk (Solid) 110 kL 6.29E-2 Ci/g 1.07E+ 01 Ci E

60Co Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 6.29E-2 Ci/g 1.07E+ 01 Ci E

60Co Sludge (Liquid

& Solid)


60Co Total 299 kL 2.91E+ 01 Ci


24


63Ni Saltcake Solid A1-SltCk (Solid) 110 kL 7.88E-1 Ci/g 1.37E+ 02 Ci E

63Ni Sludge (Liquid

& Solid)


63Ni Sludge (Liquid

& Solid)

AR (Solid) 79 kL 7.51E+ 00 Ci/g 7.95E+ 02 Ci E

63Ni Total 299 kL 1.02E+ 03 Ci

79Se Saltcake Solid A1-SltCk (Solid) 110 kL 8.45E-4 Ci/g 1.47E-1 Ci E

79Se Sludge (Liquid

& Solid)


79Se Sludge (Liquid

& Solid)


79Se Total 299 kL 2.87E-1 Ci

90Sr Saltcake Solid A1-SltCk (Solid) 110 kL 9.60E+ 02 Ci/g 1.64E+ 05 Ci E

90Sr Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 9.60E+ 02 Ci/g 1.64E+ 05 Ci E

90Sr Sludge (Liquid

& Solid)


90Sr Total 299 kL 4.45E+ 05 Ci

90Y Saltcake Solid A1-SltCk (Solid) 110 kL 9.60E+ 02 Ci/g 1.64E+ 05 Ci C

90Y Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 9.60E+ 02 Ci/g 1.64E+ 05 Ci C

90Y Sludge (Liquid

& Solid)

AR (Solid) 79 kL 9.60E+ 02 Ci/g 1.18E+ 05 Ci C

90Y Total 299 kL 4.45E+ 05 Ci Referenced to 90Sr

93Zr Saltcake Solid A1-SltCk (Solid) 110 kL 2.25E-2 Ci/g 3.91E+ 00 Ci E


25


93Zr Sludge (Liquid

& Solid)


93Zr Sludge (Liquid

& Solid)


93Zr Total 299 kL 7.62E+ 00 Ci

93mNb Saltcake Solid A1-SltCk (Solid) 110 kL 1.92E-2 Ci/g 3.34E+ 00 Ci E

93mNb Sludge (Liquid

& Solid)


93mNb Sludge (Liquid

& Solid)


93mNb Total 299 kL 6.48E+ 00 Ci

99Tc Saltcake Solid A1-SltCk (Solid) 110 kL 3.20E-1 Ci/g 5.45E+ 01 Ci E

99Tc Sludge (Liquid

& Solid)


99Tc Sludge (Liquid

& Solid)


99Tc Total 299 kL 1.48E+ 02 Ci

106Ru Saltcake Solid A1-SltCk (Solid) 110 kL 6.24E-10 Ci/g 1.08E-7 Ci E

106Ru Sludge (Liquid

& Solid)


106Ru Sludge (Liquid

& Solid)


106Ru Total 299 kL 6.19E-5 Ci

113mCd Saltcake Solid A1-SltCk (Solid) 110 kL 3.86E-2 Ci/g 6.70E+ 00 Ci E

113mCd Sludge (Liquid

& Solid)



26


113mCd Sludge (Liquid

& Solid)


113mCd Total 299 kL 9.72E+ 00 Ci

125Sb Saltcake Solid A1-SltCk (Solid) 110 kL 5.97E-4 Ci/g 1.04E-1 Ci E

125Sb Sludge (Liquid

& Solid)


125Sb Sludge (Liquid

& Solid)


125Sb Total 299 kL 1.11E+ 01 Ci

126Sn Saltcake Solid A1-SltCk (Solid) 110 kL 1.70E-3 Ci/g 2.96E-1 Ci E

126Sn Sludge (Liquid

& Solid)


126Sn Sludge (Liquid

& Solid)


126Sn Total 299 kL 5.80E-1 Ci

129I Saltcake Solid A1-SltCk (Solid) 110 kL 1.36E-4 Ci/g 2.32E-2 Ci E

129I Sludge (Liquid

& Solid)


129I Sludge (Liquid

& Solid)


129I Total 299 kL 6.32E-2 Ci

134Cs Saltcake Solid A1-SltCk (Solid) 110 kL 2.36E-5 Ci/g 4.11E-3 Ci E

134Cs Sludge (Liquid

& Solid)



& Solid)


134Cs Total 299 kL 2.70E-2 Ci


27


137Cs Saltcake Solid A1-SltCk (Solid) 110 kL 1.26E+ 02 Ci/g 2.16E+ 04 Ci E


& Solid)



& Solid)


137Cs Total 299 kL 5.86E+ 04 Ci

137mBa Saltcake Solid A1-SltCk (Solid) 110 kL 1.19E+ 02 Ci/g 2.04E+ 04 Ci C

137mBa Sludge (Liquid

& Solid)


137mBa Sludge (Liquid

& Solid)


137mBa Total 299 kL 5.53E+ 04 Ci Referenced to 137Cs

151Sm Saltcake Solid A1-SltCk (Solid) 110 kL 7.44E+ 00 Ci/g 1.29E+ 03 Ci E

151Sm Sludge (Liquid

& Solid)


151Sm Sludge (Liquid

& Solid)


151Sm Total 299 kL 3.10E+ 05 Ci .

152Eu Saltcake Solid A1-SltCk (Solid) 110 kL 1.13E-3 Ci/g 1.96E-1 Ci E

152Eu Sludge (Liquid

& Solid)



& Solid)


152Eu Total 299 kL 5.48E+ 01 Ci

154Eu Saltcake Solid A1-SltCk (Solid) 110 kL 6.85E-2 Ci/g 1.19E+ 01 Ci E


28



& Solid)



& Solid)


154Eu Total 299 kL 3.42E+ 03 Ci

155Eu Saltcake Solid A1-SltCk (Solid) 110 kL 2.02E-2 Ci/g 3.51E+ 00 Ci E


& Solid)



& Solid)


155Eu Total 299 kL 1.07E+ 03 Ci

226Ra Saltcake Solid A1-SltCk (Solid) 110 kL 4.24E-8 Ci/g 7.36E-6 Ci E

226Ra Sludge (Liquid

& Solid)



& Solid)


226Ra Total 299 kL 1.03E-5 Ci

227Ac Saltcake Solid A1-SltCk (Solid) 110 kL 9.51E-6 Ci/g 1.65E-3 Ci E

227Ac Sludge (Liquid

& Solid)


227Ac Sludge (Liquid

& Solid)


227Ac Total 299 kL 1.67E-3 Ci

228Ra Saltcake Solid A1-SltCk (Solid) 110 kL 6.13E-8 Ci/g 1.07E-5 Ci C


& Solid)

SRR (Solid) 110 kL 9.72E-14 Ci/g 1.61E-11 Ci C


29



& Solid)

AR (Solid) 79 kL 1.61E-8 Ci/g 1.71E-6 Ci C

228Ra Total 299 kL 1.24E-5 Ci

229Th Saltcake Solid A1-SltCk (Solid) 110 kL 1.69E-8 Ci/g 2.94E-6 Ci E

229Th Sludge (Liquid

& Solid)



& Solid)


229Th Total 299 kL 3.62E-6 Ci

231Pa Saltcake Solid A1-SltCk (Solid) 110 kL 4.62E-5 Ci/g 8.03E-3 Ci E

231Pa Sludge (Liquid

& Solid)


231Pa Sludge (Liquid

& Solid)


231Pa Total 299 kL 8.07E-3 Ci

232Th Saltcake Solid A1-SltCk (Solid) 110 kL 6.13E-8 Ci/g 1.07E-5 Ci E


& Solid)



& Solid)


232Th Total 299 kL 1.24E-5 Ci

232U Saltcake Solid A1-SltCk (Solid) 110 kL 3.68E-5 Ci/g 6.28E-3 Ci C

232U Sludge (Liquid

& Solid)


232U Sludge (Liquid

& Solid)



30


232U Total 299 kL 6.55E-3 Ci Based on UTOTAL

and Template isotopic

distribution ratios


233U Sludge (Liquid

& Solid)


233U Sludge (Liquid

& Solid)




distribution ratios


234U Sludge (Liquid

& Solid)


234U Sludge (Liquid

& Solid)




distribution ratios


235U Sludge (Liquid

& Solid)


235U Sludge (Liquid

& Solid)




distribution ratios



31


236U Sludge (Liquid

& Solid)


236U Sludge (Liquid

& Solid)




distribution ratios

237Np Saltcake Solid A1-SltCk (Solid) 110 kL 8.72E-4 Ci/g 1.52E-1 Ci E

237Np Sludge (Liquid

& Solid)


237Np Sludge (Liquid

& Solid)


237Np Total 299 kL 2.26E-1 Ci

238Pu Saltcake Solid A1-SltCk (Solid) 110 kL 8.86E-2 Ci/g 1.51E+ 01 Ci C

238Pu Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 8.92E-2 Ci/g 1.52E+ 01 Ci C


& Solid)

AR (Solid) 79 kL 7.11E-2 Ci/g 8.71E+ 00 Ci C

238Pu Total 299 kL 3.90E+ 01 Ci Based on 239Pu and

Template isotopic

distribution ratios.


238U Sludge (Liquid

& Solid)


238U Sludge (Liquid

& Solid)



32




distribution ratios

239Pu Saltcake Solid A1-SltCk (Solid) 110 kL 2.22E+ 00 Ci/g 3.79E+ 02 Ci C


& Solid)



& Solid)


239Pu Total 299 kL 1.03E+ 03 Ci Based on 239/240Pu



240Pu Saltcake Solid A1-SltCk (Solid) 110 kL 5.15E-1 Ci/g 8.79E+ 01 Ci C


& Solid)

SRR (Solid) 110 kL 5.15E-1 Ci/g 8.79E+ 01 Ci C


& Solid)

AR (Solid) 79 kL 4.89E-1 Ci/g 5.99E+ 01 Ci C

240Pu Total 299 kL 2.36E+ 02 Ci Based on 239/240Pu



241Am Saltcake Solid A1-SltCk (Solid) 110 kL 1.29E+ 00 Ci/g 2.19E+ 02 Ci E

241Am Sludge (Liquid

& Solid)



& Solid)


241Am Total 299 kL 5.86E+ 02 Ci

241Pu Saltcake Solid A1-SltCk (Solid) 110 kL 3.31E+ 00 Ci/g 5.64E+ 02 Ci C


33



& Solid)



& Solid)


241Pu Total 299 kL 1.37E+ 03 Ci Based on 239Pu and

Template isotopic


242Cm Saltcake Solid A1-SltCk (Solid) 110 kL 1.01E-3 Ci/g 1.73E-1 Ci C

242Cm Sludge (Liquid

& Solid)



& Solid)


242Cm Total 299 kL 4.10E-1 Ci Based on 241Am and

Template isotopic


242Pu Saltcake Solid A1-SltCk (Solid) 110 kL 3.86E-5 Ci/g 6.57E-3 Ci C


& Solid)



& Solid)


242Pu Total 299 kL 1.56E-2 Ci Based on 239Pu and

Template isotopic


243Am Saltcake Solid A1-SltCk (Solid) 110 kL 6.98E-4 Ci/g 1.19E-1 Ci C


& Solid)



& Solid)



34


243Am Total 299 kL 3.06E-1 Ci Based on 241Am and

Template isotopic




& Solid)



& Solid)



Template isotopic




& Solid)



& Solid)



Template isotopic



35

Tank 241-A-106 Best Basis Inventory Without Details -- Supplementals

Decayed To: January 1, 2008

Effective Date: October 1, 2005

Published On: February 29, 2008

Best Basis Derivation

The water concentration is applicable to the time of sampling and may change with time; no water inventory is calculated.


Ag Saltcake Solid A1-SltCk (Solid) 110 kL 3.86E+ 02 g/g 6.58E+ 01 kg E

Ag Sludge (Liquid

& Solid)


Ag Sludge (Liquid

& Solid)


Ag Total 299 kL 1.79E+ 02 kg .

B Saltcake Solid A1-SltCk (Solid) 110 kL 2.62E+ 01 g/g 4.46E+ 00 kg E

B Sludge (Liquid

& Solid)


B Sludge (Liquid

& Solid)


B Total 299 kL 1.21E+ 01 kg .

Ba Saltcake Solid A1-SltCk (Solid) 110 kL 2.30E+ 03 g/g 3.91E+ 02 kg E

Ba Sludge (Liquid

& Solid)


Ba Sludge (Liquid

& Solid)


Ba Total 299 kL 1.06E+ 03 kg .

http://twinswhse.pnl.gov/tcr.nsf/d96c5d01e8ba69e08825647b0070bd5a/17F1DA91716ADFE788256B0A0055B795/$FILE/Tank%20A-106%20TIR8%20FY06%20Q1%20-%20Final%20Rev%201.doc


36


Cd Saltcake Solid A1-SltCk (Solid) 110 kL 5.36E+ 01 g/g 9.13E+ 00 kg E

Cd Sludge (Liquid

& Solid)


Cd Sludge (Liquid

& Solid)


Cd Total 299 kL 2.48E+ 01 kg .

Co Saltcake Solid A1-SltCk (Solid) 110 kL 1.88E+ 01 g/g 3.20E+ 00 kg E

Co Sludge (Liquid

& Solid)


Co Sludge (Liquid

& Solid)


Co Total 299 kL 8.70E+ 00 kg .

Cu Saltcake Solid A1-SltCk (Solid) 110 kL 1.16E+ 02 g/g 1.99E+ 01 kg E

Cu Sludge (Liquid

& Solid)


Cu Sludge (Liquid

& Solid)


Cu Total 299 kL 5.40E+ 01 kg

Mg Saltcake Solid A1-SltCk (Solid) 110 kL 3.95E+ 03 g/g 6.74E+ 02 kg E

Mg Sludge (Liquid

& Solid)


Mg Sludge (Liquid

& Solid)


Mg Total 299 kL 1.83E+ 03 kg .

Free OH Saltcake Solid A1-SltCk (Solid) 110 kL 3.01E+ 01 g/g 5.63E+ 00 kg C


37


Free OH Sludge (Liquid

& Solid)

AR (Solid) 79 kL 3.01E+ 01 g/g 4.04E+ 00 kg C

Free OH Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 3.01E+ 01 g/g 5.63E+ 00 kg C

Free OH Total 299 kL 1.53E+ 01 kg

Aroclors

(Total

PCB)

Saltcake Solid A1-SltCk (Solid) 110 kL 2.50E+ 01 g/g 4.67E+ 00 kg E

Aroclors

(Total

PCB)

Sludge (Liquid

& Solid)


Aroclors

(Total

PCB)

Sludge (Liquid

& Solid)


Aroclors

(Total

PCB)

Total 299 kL 1.27E+ 01 kg

Th Saltcake Solid A1-SltCk (Solid) 110 kL 5.57E-1 g/g 9.67E-2 kg E

Th Sludge (Liquid

& Solid)

AR (Solid) 79 kL 1.47E-1 g/g 1.55E-2 kg E

Th Sludge (Liquid

& Solid)

SRR (Solid) 110 kL 8.82E-7 g/g 1.47E-7 kg E

Th Total 299 kL 1.12E-1 kg

239/240Pu Saltcake Solid A1-SltCk (Solid) 110 kL 2.74E+ 00 Ci/g 4.67E+ 02 Ci E

239/240Pu Sludge (Liquid

& Solid)


239/240Pu Sludge (Liquid

& Solid)



38


239/240Pu Total 299 kL 1.27E+ 03 Ci Supplemental analyte

used to calculate Pu

isotopes.

The water concentration is applicable to the time of sampling and may change with time; no water inventory is calculated.


39

Tank 241-A-106 Analytical Methods and Procedures

No data available


40

Tank 241-A-106 Subsampling Scheme and Sample Description

No report available


41

241-A-106 Sample Breakdown Diagrams

No data available


42

241-A-106 Rheology Report

No data available


43

241-A-106 Means and Confidence Intervals

Solid Data

No data available


44

241-A-106 Means and Confidence Intervals

Liquid Data

No data available


45

Tank 241-A-106 Transfers (1994 to present)

No transfers


46

241-A-106 HTCE Surface Levels


47

241-A-106 Average Monthly Tank Surface Level (after 1/1/96 only)

24

27

30

33

1/96

1/97

1/98

1/99

1/00

1/01

1/02

1/03

1/04

1/05

1/06

1/07

1/08

1/09

N

OT

E:

Mea

sure

d d

ata

poin

ts a

re i

ndic

ated

by

dots

.

N

OT

E:

Pote

nti

al o

utl

iers

due

to e

quip

men

t ca

libra

tion a

nd

mal

funct

ion.

N

OT

E:

Abru

pt

surf

ace

level

shif

ts m

ay b

e due

to r

e-b

asel

inin

g

surv

eill

ance

inst

rum

enta

tion.

Level in Inches

Surf

ace

Lev

el D

ata


48

241-A-106 Tank Temperature Profile


49

241-A-106 Core Profiles

No data available


68

Tank 241-A-106 Dilution and Mixing Studies

No data available


69


Acronym Definition

% percent

1C first cycle decontamination waste

AEA alpha energy analysis

ANOVA analysis of variance

AT alpha total

BBI Best-basis inventory

BBIM Best-basis inventory maintenance

BD below detection limit

BNFL British Nuclear Fuel Limited, Inc.

BPE barometric pressure estimate

Btu/hr British thermal units per hour

BYSltCk saltcake blend from ITS in BY Tank Farm

CAS Chemical Abstract Services

CC concentrated complexant

CEO change engineering order

CGM combustible gas meter

CHG CH2M Hill Hanford Group, Inc.

Ci curies

CI confidence interval

Ci/g curies per gram

Ci/L curies per liter

cm centimeter

cm3 cubic centimeter

cP centipoise

CRW1 REDOX cladding waste

CWHT concentrated waste holding tank

DCB decachlorobyphenyl

df degrees of freedom

dl drainable liquid

DOE U.S. Department of Energy

DQO data quality objectives

DSA data source access

DSC differential scanning calorimetry

DSS double-shell slurry

DSSF double-shell slurry feed


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Acronym Definition

DST double-shell tank

E engineering assessment-based

EB evaporator bottoms

Ecology Washington State Department of Ecology

EVAP evaporator feed waste

FIC Food Instrument Corporation

FP fission product waste from cesium and strontium recovery in B-Plant

ft feet

ft2 square feet

ft3/hr cubic feet per hour

ft3/min cubic feet per minute

g gram

g/cc grams per cubic centimeter

g/cm3 grams per cubic centimeter

g/gal grams per gallon

g/L grams per liter

g/mL grams per milliliter

GC gas chromatographs

GCS gas characterization system

GEA gravimetric energy analysis

GRE gas release event

C/mL micrograms of carbon per milliliter

Ci/g microcuries per gram

Ci/gal microcuries per gallon

Ci/L microcuries per liter

Ci/mL microcuries per milliliter

eq/g microequivalents per gram

eq/mL microequivalents per milliliter

g microgram

g/g micrograms per gram

g/ml micrograms per milliliter

gC/g micrograms of carbon per gram

mol micromole

mol/L micromoles per liter


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Acronym Definition

HDW Hanford defined waste

HHF Hydrostatic head fluid

HLAN Hanford local area network

HTCE historical tank content estimate

IC ion chromatography

ICP inductively coupled plasma spectroscopy

ICP/AES inductively coupled plasma/atomic emission spectrometry

ICP/MS inductively coupled plasma/mass spectroscopy

IH Industrial Hygiene

in. inch

IS insufficient sample

ITS in-tank solidification

IX ion exchange waste

J/g joules per gram

kg kilogram

kgal kilogallon

kL kiloliter

kW kilowatt

LANL Los Alamos National Laboratory

LAW low activity waste

LCS laboratory control standard

LEL lower explosive limit

LFL lower flammability limit

LH lower half

LL lower limit

LMHC Lockheed Martin Hanford Corporation

LOI letter of instruction

LOW liquid observation well

m meter

M Hanford defined waste model-based

M/L moles per liter

MDA minimum detectable activity

mg milligram

mg/L milligrams per liter

mg/m3 milligrams per cubic meter


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Acronym Definition

MIT multi-functional instrument tree

mL milliliter

mm millimeter

MOU memorandum of understanding

mRad/hr millirad per hour

MRQ minimum reportable quantity

m2 square meter

m3 cubic meter

m3/hr cubic meters per hour

MW metal waste

n/a not applicable

n/d not detected

n/d not determined

N/D not determined

n/r not reported

NA not available

NCPLX non-complexed

NF not found

NR not reported

NR not required

NR not requested

ORNL Oak Ridge National Laboratory

ORP Office of River Protection

OVM organic vapor monitor

OWW organic wash waste

PCB polychlorinated biphenyl

pH potential of hydrogen

PHMC Project Hanford Management Contractor

PNNL Pacific Northwest National Laboratory

ppm parts per million

ppmv parts per million by volume

PRSST propagating reactive system screening test

PUREX Plutonium Uranium Extraction

QC quality control

R1 REDOX high-level waste generated from 1952 to 1957


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Acronym Definition

rad/hr radiation absorbed dose per hour

REDOX Reduction and Oxidation

REML restricted maximum likelihood estimation methods

RGS retained gas sampler

RPD relative percent difference

RPP River Protection Project

RR re-run

RSD relative standard deviation

S sample-based

SACS Surveillance Analysis Computer System

SAP sampling and analysis plan

SD standard deviation

SHMS standard hydrogen monitoring systems

SMM supernatant mixing model

SMMS supernatant mixing model saltcake

SMMS1 SMM 242-S evaporator saltcake generated from 1973 until 1976

SMMS2 SMM 242-S evaporator saltcake generated from 1977 until 1980

SpG specific gravity oC degrees centigrade

oF degrees Fahrenheit

SST single-shell tank

STP standard temperature and pressure

SU supernatant

SVOA semi-volatile organic analysis

SWLIQ dilute, non-complexed waste from 200-E Area single-shell tanks

T1SltCk 242-T evaporator saltcake waste, 1951 to 1955

TB total beta

TBP tributyl phosphate

TCD tank characterization database

TCP tank characterization plan

TCR tank characterization report

TCX tetrachloro-m-xylene

TGA thermogravimetric analysis

TIC total inorganic carbon

TIR tank interpretive report


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Acronym Definition

TLM tank layer model

TOC total organic carbon

TRU transuranic

TSAP Tank Sampling and Analysis Plan

TWINS Tank Waste Information Network System

TWRS Tank Waste Remediation System

UH upper half

UL upper limit

VFI void fraction instrument

VIDON Visual Image Digital Object Network

vol% volume percent

VSS vapor sampling system

W watts

W/Ci watts per curie

W/L watts per liter

WHC Westinghouse Hanford Company

WIT Waste Disposal Integration Team

WSTRS waste status and transaction record summary

wt% weight percent

Eo-...RPP-RPT-42744, Rev.0 1 2009 Auto-TCR for Tank 241-A-106 _____ Some of the reports herein may...

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Transcript of Eo-...RPP-RPT-42744, Rev.0 1 2009 Auto-TCR for Tank 241-A-106 _____ Some of the reports herein may...