cleanup status report no. 30 - period of september 24 … · cleanup status report no. 30 –...

FAP_CLEANUP STATUS REPORT NO 30.DOC 1 FEBRUARY 2011 ES021411044224DFW\110450047

T E C H N I C A L M E M O R A N D U M – F I N A L

Cleanup Status Report – No. 30 Period of September 24 to December 24, 2010 Fruit Avenue Plume Superfund Site Long-term Remedial Action (LTRA)

PREPARED FOR: Bartolomé Cañellas/EPA Sabino Rivera/NMED Alex Mora/CoA Barbara Gastian/ABCWUA

PREPARED BY: CH2M HILL COPY TO: Brian Wied/CH2M HILL

Scott McKinley/CH2M HILL William LeFevre/CH2M HILL

PREPARED UNDER: EPA Region 6 Response Action Contract No. EP-W-06-021 Task Order 0003-RALR-06DD

DCN: 0003-02073 DATE: February 15, 2010

1. Introduction This cleanup status report (CSR) summarizes long-term remedial action (LTRA) operations and maintenance (O&M) activities and monitoring data for the pump and treat (P&T) system operated as part of the selected remedy for the Fruit Avenue Plume Superfund Site (Site; Comprehensive Environmental Response, Compensation, and Liability Information System [CERCLIS] No. NMD986668911). Additional information on the contaminants of concern (COC), P&T system configuration, well locations, and system layout can be obtained from CSR No.26 (CH2M HILL, 2009a). A summary of startup operations may be found in CSR No. 1 (CH2M HILL, 2005). This report (CSR No. 30) describes activities performed on the P&T system from September 24 through December 24, 2010.

The Fruit Avenue Plume Superfund Site Record of Decision (U.S. Environmental Protection Agency, [EPA], 2001) established a remedial action objective (RAO) for the Site to prevent human ingestion of, inhalation of, or dermal contact with groundwater that contains trichloroethene (TCE) concentrations above 5 micrograms per liter (µg/L), and other COCs at concentrations greater than their corresponding maximum contaminant levels (MCL), as promulgated by the Clean Water Act (40 Code of Federal Regulations 141.61, “National Primary Drinking Water Regulations, Maximum Contaminant Levels for Organic Contaminants”). Currently, TCE is the only COC that exceeds its 5 µg/L RAO for the Site.

FRUIT AVENUE PLUME SUPERFUND SITE CLEANUP STATUS REPORT NO. 30 – SEPTEMBER 24, 2010 TO DECEMBER 24, 2010

FINAL


To help meet this RAO and other applicable or relevant and appropriate requirements, the P&T system has the following operational goals:

• Operate the air stripper treatment plant (ASTP) to remove COCs from extracted groundwater to concentrations lower than their MCLs or non-zero maximum contaminant level goals before returning the treated water to the aquifer.

• Operate the ASTP to maintain COCs in the air stripper offgas at concentrations below state and federal threshold levels.

• Maintain the P&T system’s run time at greater than 80 percent when continuous or pulsed run mode operations are underway.

The third operational goal was recently modified as described in the RSE Report (CH2M HILL, 2009b), which recommended pulsed operation of the P&T system. The decision to start or stop the system during pulsed operations is based on evaluation of COC concentration rebound and plume mobility criterion also described in the RSE Report (CH2M HILL, 2009b).

2. Field Activities This section summarizes the field activities (see Attachment 1) and operational data (see Attachment 2) that were collected during this reporting period. Operational highlights for this reporting period are presented in Table 1, and a summary of O&M activities is presented in Table 2. ASTP performance was monitored by the operations staff during site visits (see Table 3), and through remote monitoring of the supervisory control and data acquisition (SCADA) system.

2.1 ASTP Operation During this reporting period, the P&T system operated nearly continuously in the run phase of the EPA-approved (CH2M HILL, 2009b) pulsed operation mode.

During the run phase, the ASTP was operated for 2,129 hours of the 2,184 hours run mode available this period (97 percent run time). The treatment rate was approximately 84 gallons per minute (gpm). The cumulative and monthly volumes of groundwater treated and reinjected by the ASTP are presented in Table 4 and Figure 1. Through the end of this reporting period, a cumulative total of approximately 151 million gallons of water have been pumped from the extraction well and treated by the ASTP. During this reporting period, approximately 10.7 million gallons of water were pumped from the extraction well and treated by the ASTP.


FINAL


Routine O&M activities performed this period consisted of changing ASTP effluent bag filters, disinfecting the reinjection system, and adjusting the acid pump stroke length. A sample port inside the ASTP, which broke and was temporarily repaired during the previous reporting period, was repaired. Water previously produced during back flushing and contained onsite in a 23,000-gallon Baker tank, was transported to an offsite facility for disposal. No other system modifications or non-routine maintenance activity were performed this reporting period.

During this run phase, the ASTP was temporarily shut down because of an acid shortage, a low pH alarm, and to repair the broken sample port. The cumulative down time was 55 hours (3 percent) of the total 2,184-hour run phase duration. The ASTP run time calculations and history are presented in Table 5.

2.2 Sampling Results Routine sampling of the ASTP influent and effluent groundwater was conducted on September 23 and December 14, 2010. Recently measured COC concentrations in the ASTP influent (sample port SP-1) and effluent (sample port SP-5) are summarized in Table 6 and illustrated in Figure 2.

The mass of COCs removed by the ASTP during this reporting period was estimated (Attachment 3) based on the total volume of groundwater pumped from the extraction well during the reporting period and the difference between the ASTP influent and treated (effluent) water COC concentrations, as measured during the December 14, 2010, sampling event. The cumulative and monthly mass of COCs removed from groundwater since the P&T system began operations are presented in Table 7 and illustrated in Figure 3. Approximately 8.32 kilograms (kg) of volatile organic compounds (VOC) (consisting of TCE, cis 1,2-dichloroethene [cis-1,2-DCE], and trans-1,2-DCE) are estimated to have been removed from the aquifer since the P&T system began operation in 2005.

3. Operations Summary Based on the monitoring and observations made during this reporting period, the following operations summary was developed:

• The treatment system was in operation for about 2,129 hours (97 percent) of the run mode period (September 24 through December 24, 2010).

• Approximately 10.7 million gallons of water were pumped from the aquifer and treated.

• An estimated 0.32 kg of total VOCs (consisting of TCE, cis-1,2-DCE, and trans-1,2-DCE) were removed from the aquifer during this reporting period.

4. Recommendations/Upcoming Activities Groundwater samples will continue to be collected from the ASTP influent and effluent while operating in the pulsed operation run mode, in accordance with schedules established in the Field Sampling Plan (CH2M HILL, 2009c). Evaluation of the laboratory analysis results will be performed to support decision making on whether to continue in run mode


FINAL


or change back to rest mode. Per the recommendations in the RSE, the system will resume run mode until there have been no significant change in the influent TCE concentration for a minimum of four sampling events when evaluated using Mann-Kendall analysis. A minimum of two additional samples will be required to complete the evaluation and these samples will be collected monthly during the January and February reporting periods, respectively. Normal system maintenance also will continue during the December 2010 through March 2011 operation period. The next quarterly reporting period will end on March 25, 2010, and the CSR will be updated and distributed for review on or about April 15, 2011.

5. Works Cited 40 CFR 141.61. “National Primary Drinking Water Regulations, Maximum Contaminant Levels for Organic Contaminants.” Code of Federal Regulations.

CH2M HILL. 2005. Cleanup Status Report No. 1 – Startup Version 1.0, April 2005, Fruit Avenue Plume Superfund Site. Albuquerque, New Mexico. January.

CH2M HILL. 2009a. Cleanup Status Report No. 26 – Version 1.0, Period of September 25, 2009, to December 24, 2009, Fruit Avenue Plume Superfund Site. Albuquerque, New Mexico.

CH2M HILL. 2009b. Remedial System Evaluation Report, Version 1.2, September 2009, Fruit Avenue Plume Superfund Site. Albuquerque, New Mexico.

CH2M HILL. 2009c. Field Sampling Plan, Version 2.0, September 2009, Fruit Avenue Plume Superfund Site. Albuquerque, New Mexico. Remedial Action Contract No. EP-W-06-021 Task Order No.0003-RALR-06D. October.

U.S. Environmental Protection Agency (EPA). 2001. Record of Decision. Fruit Avenue Plume Site. Albuquerque, New Mexico. CERCLIS No. NMD986668911.

Abbreviations and Acronyms

FRUIT AVENUE PLUME SUPERFUND SITE CLEANUP STATUS REPORT NO. 30 - SEPTEMBER 24, 2010, TO DECEMBER 24, 2010

FINAL

FAP_CLEANUP STATUS REPORT NO 30.DOC FEBRUARY 2011 ES021411044224DFW\110450047

(This page intentionally left blank)


Abbreviations and Acronyms

µg/L micrograms per liter

ARAR applicable or relevant and appropriate requirement

ASTP air stripper treatment plant

CERCLIS Comprehensive Environmental Response, Compensation, and Liability Information System

Cis 1,2-DCE cis 1,2-dichloroethene

COC contaminant of concern

CSR cleanup status report

DCE dichloroethene

EPA U.S. Environmental Protection Agency

gpm gallons per minute

HMI human-machine interface

kg kilogram

LTRA long-term remedial action

MCLG maximum contaminant level goal

MCL maximum contaminant level

O&M operations and maintenance

P&T pump and treat

RAO remedial action objective

SCADA supervisory control and data acquisition

Site Fruit Avenue Plume Superfund Site

TCE trichloroethene

VOC volatile organic compound


FINAL



Tables


FINAL



TABLE 1ASTP Operational Highlights (September 24, 2010 to December 24, 2010)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

October November December TotalReporting Period Start Date 9/24/10 12:00 10/29/10 13:30 11/26/10 12:00 9/24/10 12:00 PMReporting Period End Datea 10/29/10 13:30 11/26/10 12:00 12/24/10 12:00 12/24/10 12:00 PMDuration of Pulsed Operation Run Mode [days] 35.1 27.9 28.0 91.0Run Time [hours] 787.13 669.48 672.00 2,128.62 Percent Operational during Pulsed Operation Period 94% 100% 100% 97%Total volume [gal] of gw treated during the reporting period 3,923,085 3,478,984 3,324,891 10,726,960 Mass [kg] of TCE and other VOCs removed 0.12 0.10 0.10 0.321Mass [lbs] of TCE and other VOCs removed 0.26 0.23 0.22 0.708aThe monthly operation period is usually terminated on the last Friday of each month.

FAP_CLEANUP STATUS REPORT NO.30.DOC ES021411044224DFW\110450047 1 OF 1 FEBRUARY 2011

Albuquerque, New MexicoDate Activity

September 24, 2010 Beginning of reporting period (12:00 Noon)September 28, 2010 Disinfect EQ tankOctober 5, 2010 Receive acid delivery - Cancel for safety reasons.October 8, 2010 Disinfect EQ tankOctober 14, 2010 ASTP Shut down for piping repair (06:40)October 15, 2010 ASTP restarted (10:40)

Backflushing water hauled off site. October 21, 2010 ASTP Shut down due to sulfuric acid shortage (09:04)

Fencing at acid tank modified, camloc fitting replaced.October 22, 2010 ASTP restarted (11:26)October 28, 2010 Adjust acid pump stroke length to 68%October 29, 2010 End of reporting period (12:00)


October 29, 2010 Beginning of reporting period (12:00 Noon)November 1, 2010 Adjust acid pump stroke length to 70%November 9, 2010 Adjust acid pump stroke length to 75%November 23, 2010 ASTP Shut down for low pH alarm (12:14).November 26, 2010 End of reporting period (12:00)


November 26, 2010 Beginning of reporting period (12:00 Noon)December 10, 2010 Acid delivery receivedDecember 14, 2010 Performance SamplingDecember 20, 2010 Change effluent bag filtersDecember 24, 2010 End of reporting period (12:00)

TABLE 2 - ConcludedASTP O&M Activities (November 26, 2010 to December 24, 2010)Fruit Avenue Plume Superfund Site

TABLE 2ASTP O&M Activities (September 24, 2010 to October 29, 2010)Fruit Avenue Plume Superfund Site

TABLE 2 - ContinuedASTP O&M Activities (October 29, 2010 to November 26, 2010)Fruit Avenue Plume Superfund Site

FAP_CLEANUP STATUS REPORT NO.30.DOCES021411044224DFW\110450047 1 OF 1 FEBRUARY 2011

TABLE 3ASTP Operational Data (September 24, 2010 to December 24, 2010)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

9/24/10 12:00 9/28/10 13:00 10/8/10 12:00 10/29/10 13:30 11/19/10 12:00 11/26/10 12:00 12/10/10 12:00 12/24/10 12:00COMPUTER CONTROL SCREEN READINGSOverview ScreenTreated Water (Injection Well) Flow FIT-3121 GPM 82.4 82.0 82.0 87.6 86.5 83.0 79.9 87.2Equalization Tank Level PIT-391 FEET 2.7 2.68 2.69 2.68 2.68 2.64 2.8 2.69Acid Tank Level LIT331 FEET 2.7 2.47 1.80 4.63 3.2 2.7 1.7 4.1Reinjection Pump Pressure PIT-3101 PSI 39.2 39.2 39.5 46.0 46.1 43.5 43.9 44.5Pumping Well Level LX-311 FEET 111.6 111.9 111.5 110.5 111.6 112.5 113.9 111.9Pumping Well Discharge Flow FIT-311 GPM 83.0 82.5 82.7 87.9 86.9 84.0 80.0 87.5Single Injection Well Pressure PIT-3131 PSI 37.2 37.1 37.3 43.6 42.4 38.3 34.7 42.6Single Injection Well Level LX-3131 FEET 151 5 151 7 151 9 153 0 153 9 153 4 153 5 154 9

UnitsEquipment IDDate & Time Date & Time Date & Time

FAP ASTP Inspection Data Log Form

Single Injection Well Level LX-3131 FEET 151.5 151.7 151.9 153.0 153.9 153.4 153.5 154.9Single Injection Well Flow FIT-3131 GPM 40.2 40.2 40.5 42.6 41.9 40.5 38.8 42.5Dual Injection Well Pressure PIT-3132 PSI 37.8 37.7 37.8 44.3 43.2 39.0 35.6 43.3Dual Injection Well Level LX-3132 FEET 99.8 100.0 100.1 101.0 102.1 102.2 102.6 103.2Dual Injection Well Flow FIT-3132 GPM 42.1 41.6 41.5 44.7 43.9 42.5 40.9 44.6pH Set point N/A mg/L 5.5 5.5 5.5 5.5 5.5 5.5 5.5 5.5Equipment Run Times ScreenAcid Feed Pump P-331 HRS 26,598.0 26,684.3 26,911.3 27,374.3 27,891.7 28,055.0 28,380.3 28,708.6Air Stripper Blower P-361 HRS 30,013.5 30,097.7 30,325.6 30,788.0 31,305.6 31,469.0 31,794.1 32,122.3Transfer Pump P-381 HRS 27,332.4 27,416.5 27,644.4 28,106.7 28,624.3 28,787.6 29,112.8 29,440.9Reinjection Pump P-3101 HRS 29,847.4 29,931.5 30,159.5 30,622.1 31,139.6 31,302.9 31,628.1 31,956.3Pumping Well Pump P-311 HRS 26,814.6 26,898.7 27,126.6 27,588.9 28,106.5 28,269.8 28,594.9 28,923.0TotalizersTotal Treated Water Flow (FIT) FIT-3121 GAL 137,494,350 137,914,039 139,064,720 141,384,333 144,015,974 144,841,183 146,501,516 148,142,018Pumping Well Flow (FIT) FIT-311 GAL 140,526,910 140,949,343 142,110,420 144,449,995 147,097,756 147,928,979 149,609,452 151,253,870Single Injection Well Flow (FIT) FIT-3131 GAL 86,198,024 86,403,433 86,969,176 88,111,489 89,393,750 89,797,846 90,611,991 91,414,228D l I j ti W ll Fl (FIT) FIT 3132 GAL 48 951 037 49 164 600 49 750 480 50 927 717 52 279 276 52 700 742 53 550 822 54 386 606Dual Injection Well Flow (FIT) FIT-3132 GAL 48,951,037 49,164,600 49,750,480 50,927,717 52,279,276 52,700,742 53,550,822 54,386,606Dual Injection Well Flow (FIT) FIT-3133 11,574,184 11,574,184 11,574,184 11,574,184 11,574,184 11,574,184 11,574,184 11,574,184LOCAL EQUIPMENT READINGSWater Utility Meter - Outside ASTP N/A Ft^3 2,058.67 2,058.67 2,058.67 2,059.86 2,059.86 2,059.86 2,059.86 2,059.86Electric Utility Meter - Outside ASTP N/A kWh 117,959 119,275 122,832 130,071 137,945 140,464 145,636 150,538Electric Utility Meter - D2EI3/D2EP1 N/A kWh 114,893 115,347 116,908 119,938 123,470 124,564 126,752 128,939Recirculation Totalizer Inside ASTP N/A GAL 1,827,928 1,827,928 1,827,928 1,827,930 1,827,928 1,827,928 1,827,930 1,827,930Pressure Gauge at ASTP Influent N/A PSI 4.0 4.0 4.3 4.2 4.6 4.2 4.3 4.2Pressure Gauge after Influent Bag Filter N/A PSI 0.0 0.0 2.5 1.2 2.0 2.6 2.9 2.4Air Stripper Blower Airflow Rate N/A x100 CFM 9.6 9.6 9.0 9.6 9.0 9.0 8.9 9.0Air Stripper Sump Pressure N/A in-H2O 15.0 15.0 15.0 15.0 15.0 15.0 15.0 15.0Pressure Gauge after Transfer Pump N/A PSI 7.2 7.0 7.8 8.0 7.7 8.1 9.0 7.0Pressure Gauge after Treated Water Bag Filter N/A PSI NA NA 34.7 41.0 38.6 35.2 32.5 40.0ACID Feed Pump Stroke Length N/A Stroke 64% 64% 64% 65% 67% 68% 66% 66%Notes:ASTP Air Stripper Treatment Plantppbgs below ground surfaceft feethrs hoursmg/L milligrams per literkWh kilowatt hourgal gallonmm micrometermL milliliterpsi pounds per square inch(1) = ASTP shut down for pulsed operations.


TABLE 4Volume of Water Extracted and Injected - 2010Fruit Avenue Plume Superfund Site Albuquerque, New Mexico

Cumulative Extraction

Monthly Extraction

Pumping Well Flow(gal)

Treated Water Flow(gal)

Single Injection Well Flow

(gal)

Dual Injection Well Upper

Flow(gal)a

Dual Injection Well Lower

Flow(gal)a

Pumping Well Flow(gal)

Treated Water Flow(gal)

Single Injection Well Flow

(gal)

Dual Injection Well Upper Flow

(gal)a

Dual Injection Well Lower Flow

(gal)a

2/26/2010 137,061,152 134,058,061 84,519,799 47,198,750 11,574,184 6,339 6,320 6,300 - - 3/26/2010 137,065,584 134,062,491 84,524,945 47,198,750 11,574,184 4,432 4,430 5,146 - - 4/30/2010 137,065,584 134,062,491 84,524,945 47,198,750 11,574,184 - - - - - 5/28/2010 137,065,584 134,062,491 84,524,945 47,198,776 11,574,184 - - - 26 - 6/25/2010 137,071,339 134,066,821 84,530,260 47,198,775 11,574,184 5,755 4,330 5,315 -1 - 7/30/2010 137,078,514 134,074,074 84,534,582 47,208,948 11,574,184 7,175 7,253 4,322 10,173 - 8/27/2010 137,282,504 134,271,842 84,627,261 47,304,320 11,574,184 203,990 197,768 92,679 95,372 - 9/24/2010 140,526,910 137,494,350 86,198,024 48,951,037 11,574,184 3,244,406 3,222,508 1,570,763 1,646,717 - 10/29/2010 144,449,995 141,384,333 88,111,489 50,927,717 11,574,184 3,923,085 3,889,983 1,913,465 1,976,680 - 11/26/2010 147,928,979 144,841,183 89,797,846 52,700,742 11,574,184 3,478,984 3,456,850 1,686,357 1,773,025 - 12/24/2010 151,253,870 148,142,018 91,414,228 54,386,606 11,574,184 3,324,891 3,300,835 1,616,382 1,685,864 -

Period End Date

Cumulative Injection Monthly Injection

aDual Injection Well Lower Flow is no longer monitored separately from the Upper Flow.


TABLE 5ASTP Run Time Calculation and History (September 24 to October 29, 2010)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Event Date/Times Cause Start 9/24/10 12:00 ASTP start 10/14/10 6:40 End 10/29/10 12:00 ASTP stop 10/15/10 10:40 Duration [days] 35.0 downtime [hrs] 28.00 Duration [hours] 840 Percent Operational 94% ASTP stop 10/21/10 9:04

restart 10/22/10 11:26downtime [hrs] 26.37

Total Downtime [hrs] 54.37 hrs

TABLE 5 - ContinuedASTP Run Time Calculation and History (October 29 to November 26, 2010)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Event Date/Times Cause Start 10/29/10 12:00 ASTP stop 11/23/10 12:14 End 11/26/10 12:00 restart 11/23/10 13:15 Duration [days] 28.0 downtime [hrs] 1.02 Duration [hours] 672 Percent Operational 100%

Total Downtime [hrs] 1.02

ASTP Run Time

Pipe repair

Rest Mode - Pulsed Ops

November 2010 Reporting PeriodRun Mode - Pulsed Ops

October 2010 Reporting Period

ASTP Downtime

Low pH Alarm

Acid Shortage


TABLE 5 - ContinuedASTP Run Time Calculation and History (November 26 to December 24, 2010)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Event Date/Times Cause Start 11/26/10 12:00 ASTP stop End 12/24/10 12:00 restart Duration [days] 28.0 downtime [hrs] 0.00 Duration [hours] 672 Percent Operational 100%

Total Downtime [hrs] 0.00

TABLE 5 - ContinuedASTP Run Time Calculation for the Reporting Period (June 25, 2010 to September 24, 2010) and HistoryFruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Run Mode Date/Times Reporting Date % Operational Operational ModeStart 9/24/10 12:00 12/24/2010 100% Run ModeStop 12/24/10 12:00 11/26/2010 100% Run ModeReporting Period [days] 91 10/29/2010 94% Run ModeReporting Period [hrs] 2184 9/24/2010 92% Run ModeSystem Downtime [hrs] 55 8/27/2010 8.0% Run & Rest ModeOperational Period [hrs] 2129 7/30/2010 0.27% Rest ModePercent Operational 97% 6/28/2010 0.18% Rest Mode

5/28/2010 0.0% Rest Mode4/30/2010 0.0% Rest Mode3/26/2010 0.29% Rest Mode2/26/2010 0.27% Rest Mode1/29/2010 0.0% Rest Mode12/30/2009 0.11% Rest Mode

12-Month Run Time HistoryJune- September Reporting Period

None

December 2010 Reporting Period ASTP DowntimeRun Mode - Pulsed Ops


TABLE 6Summary Analytical Results From Recent Influent and Effluent Water SamplingFruit Avenue Plume Superfund Site Albuquerque, New Mexico

Date

cis-1,2-Dichloroethene

[µg/L] Q

trans-1,2-Dichloroethene

[µg/L] Q

Trichloro-ethene[µg/L] Q

February 2010FAP SP-1-Q110a N Influent 2/1/10 2.0 0.6 5.5FAP SP-1 DUP-Q110a QA/QC Influent 2/1/10 2.2 0.6 5.6March 2010FAP SP-1a N Influent 3/18/10 1.8 0.6 5.0FAP SP-1 DUPa QA/QC Influent 3/18/10 1.8 0.6 5.0June 2010FAP SP-1a N Influent 6/22/10 1.9 0.6 5.3FAP SP-1 DUPa QA/QC Influent 6/22/10 2 0.6 5.5July 2010FAP SP-1a N Influent 7/26/10 2.0 0.58 6.3FAP SP-1 DUPa QA/QC Influent 7/26/10 2.0 0.55 6.4September 2010FAP SP-1a N Influent 9/23/10 1.6 0.5 U 4.4FAP SP-1 DUPa QA/QC Influent 9/23/10 1.5 0.5 U 4.2FAP SP-5b N Effluent 9/23/10 0.5 U 0.5 U 0.5 UDecember 2010FAP SP-1a N Influent 12/14/10 2.3 0.66 5.7FAP SP-1 DUPa QA/QC Influent 12/14/10 2.4 0.69 5.9FAP SP-5b N Effluent 12/14/10 0.5 U 0.5 U 0.5 UNotes: Data Qualifier (Q):aSample taken from sample port at ASTP influent line (SP1) U - the analyte was not detectedbSample taken from sample port after treated water bag filter (SP5)Shaded cells indicate detected analytesN - normal sample. QA/QC - quality assurance and quality control sample.µg/L - micrograms per literOnly analytical results for COCs are included in this table.

Sample Type& LocationSample ID

FAP_CLEANUP STATUS REPORT NO.30.DOC ES021411044224DFW\110450047

1 OF 1 FEBRUARY 2011

Albuquerque, New Mexico

Date

Monthly TCE Removed

(kg)

Monthly cDCE Removed

(kg)

Monthly tDCE Removed

(kg)

Monthly COC Removal

(kg)

Cumulative TCE Removed

(kg)

Cumulative cDCE Removed

(kg)

Cumulative tDCE Removed

(kg)

Cumulative COC Removal

(kg)2/26/2010 0.000 0.000 0.000 0.00 5.25 2.01 0.633 7.893/26/2010 0.000 0.000 0.000 0.00 5.25 2.01 0.633 7.894/30/2010 0.000 0.000 0.000 0.00 5.25 2.01 0.633 7.895/28/2010 0.000 0.000 0.000 0.00 5.25 2.01 0.633 7.896/25/2010 0.000 0.000 0.000 0.00 5.25 2.01 0.633 7.897/30/2010 0.000 0.000 0.000 0.00 5.25 2.01 0.633 7.898/27/2010 0.005 0.001 0.000 0.01 5.25 2.01 0.633 7.899/24/2010 0.076 0.021 0.004 0.10 5.33 2.03 0.637 8.0010/29/2010 0.081 0.030 0.006 0.12 5.41 2.06 0.643 8.1111/26/2010 0.072 0.027 0.005 0.10 5.48 2.09 0.648 8.2212/24/2010 0.069 0.026 0.005 0.10 5.55 2.12 0.653 8.32

Note:

TABLE 7COC Mass Removed - 2010Fruit Avenue Plume Superfund Site

The ASTP was shut down from 7/15/2009 through 8/24/2010

FAP_CLEANUP STATUS REPORT ES021411044224DFW\110450047 1 OF 1 FEBRUARY 2011

Figures


FINAL



FIGURE 1 Monthly and Cumulative Volume of Treated Water ReinjectedFruit Avenue Superfund SiteAlbuquerque, NM

ES060910183634WDC

Jan-

05

Apr-0

5

Jul-0

5

Oct-05

Jan-

06

Apr-0

6

Jul-0

6

Oct-06

Jan-

07

Apr-0

7

Jul-0

7

Oct-07

Jan-

08

Apr-0

8

Jul-0

8

Oct-08

Jan-

09

Apr-0

9

Jul-0

9

Oct-09

Jan-

10

Apr-1

0

Jul-1

0

Oct-10

Vol

ume

of W

ater

[mill

ion

gallo

ns]

0

20

40

60

80

100

120

140

160Cumulative Treated Water Injected

Jan-

05

Apr-0

5

Jul-0

5

Oct-05

Jan-

06

Apr-0

6

Jul-0

6

Oct-06

Jan-

07

Apr-0

7

Jul-0

7

Oct-07

Jan-

08

Apr-0

8

Jul-0

8

Oct-08

Jan-

09

Apr-0

9

Jul-0

9

Oct-09

Jan-

10

Apr-1

0

Jul-1

0

Oct-10

Vol

ume

of W

ater

[mill

ion

gallo

ns]

0

1

2

3

4

5Monthly Treated Water Injected

FIGURE 2 TCE Concentration in Untreated Influent GroundwaterFruit Avenue Superfund SiteAlbuquerque, NM

ES060910183634WDC

2005 2006 2007 2008 2009 2010 2011 2012

Con

tam

inan

t Con

cent

ratio

n [

g/L]

0

2

4

6

8

10

12

14

16

Field Data

USEPA MCL for TCE

Run Rest RunMode Mode Mode

FIGURE 3 Monthly and Cumulative Containment Mass RemovalFruit Avenue Superfund SiteAlbuquerque, NM

ES060910183634WDC

Jan-

05

Apr-0

5

Jul-0

5

Oct-05

Jan-

06

Apr-0

6

Jul-0

6

Oct-06

Jan-

07

Apr-0

7

Jul-0

7

Oct-07

Jan-

08

Apr-0

8

Jul-0

8

Oct-08

Jan-

09

Apr-0

9

Jul-0

9

Oct-09

Jan-

10

Apr-1

0

Jul-1

0

Oct-10

Cum

ulat

ive

Mas

s R

emov

ed [k

g]

0

2

4

6

8

10Cumulative TCE Removed Cumulative cDCE Removed Cumulative tDCE Removed Cumulative Total COCs Removed

Jan-

05

Apr-0

5

Jul-0

5

Oct-05

Jan-

06

Apr-0

6

Jul-0

6

Oct-06

Jan-

07

Apr-0

7

Jul-0

7

Oct-07

Jan-

08

Apr-0

8

Jul-0

8

Oct-08

Jan-

09

Apr-0

9

Jul-0

9

Oct-09

Jan-

10

Apr-1

0

Jul-1

0

Oct-10

Mon

thly

Mas

s R

emov

ed [k

g]

0.0

0.1

0.2

0.3

0.4

Monthly TCE Removed Monthly cDCE Removed Monthly tDCE Removed Monthly Total COCs Removed


FINAL



Attachment 1 Field Notes


FINAL



\ ,\V/

/'\,.x0 :'iJ) ,'" ,. Sv,,.--} Z'6 -1 'ld\ 1) .

~:!o =l~~~~~~/~ ~~0%IU~~tQO -- - . --- --- - - -- - - - - -- - - ----- - - - - - - -

OC+6~v ~ '2£)10.. . (> 6o~~-\f~ l?5L ~~tr?2-~ i,vc1 ~(;t~'J 0.(53'0 . ~_,.",.., ~0",," .'''J"'iv4_

~-",,",- ~ s ~ .~ JZLe-s~·~

oj t3w.h...vc- M ' '-It-w.. <u,'cl +v-..kA<...

u.J h~c Ie ~f' . -Iv ~ s ~ Sl"'y<f.

~.f4<'-- {) I.kl rhJ'~7 L", . ."I/

~'-u. /t..' /""'~L ~ 1..,;$.<--, l)Js·~ a tcJ.cd~.s ~ ~:.... ~ir (..~"""-'"-.fir~<-"

~Ix/~) , CewtlG/''''-4.. ~- "<-' ----'~ Ii---~ ....... ~A-f ,",-",,,-li../f:Is ".Go/- ,:...."..-- c:Mj ~Ob - 78b 'J,y'I"'~ ;"v'~{ i pfl k'"-<>~.

'*~ (~ '?t ~:;. .... ~ I 'S<-< J,4-""'-v/a-( J,· !qe N.~ f2J.VU-'(J-- .iffi""pJ.v;J'U<.. -+ ."''''' ....... ~ J: >~L"'- !cxftu.b.~. iN. 1 .... ~.J' ;1-f.c,l-pr t&.~ .. ~ -~ ;:yV 4 v"..tK.,

0'Blf-D ~r).-..vc. ckc;cI. .... , 7:0 ~ -jt.. ...... ~(:l.i <cV.j _

DoW rOf)kl l~ Vf ~ .1'0 , &"1\ Jl}+''j .J",em- Q.bYVI:) ~ ~~:8ck ffl"'J 4~/~d ./?e::x. f.r.:1.

. C:~;~~ . ~ ~';;(f)"" iJvk-~ ~ 6le. {!.1)f,6t-- geIJlJ'9,

:Co

" " "

-,

--

10(21/&610 ~ @ ft-rfJ ~ :?'~ ;1c;)J &p~ .. u11 /J..J(k1--, _ (

)

. / Z zj-z.0/ & t5z. C)""vv"-S-:T~; (J.:vd ~.Ir"~ ItY~ - J)rvv.-.- "'';'V'-P{ (rt-/- J~

, /J-<4Y r!wAo"L /#'"'Jt ~.dUt ~d~ ,t ~-.£.¥ <Uris ~. ;()-y{I (.~ iJ_'v~ ~ .. --'e

f/ a;)I..- '(J- ., .-.."........,.t """""'-

/I:PS" ?0 .~~/r/ ~ ~,~c" h u",/oa.t ~.vv-,

//.'(/ j~a..d"--l IJ//~J. 1".-, ~ ~~ 110-);'"

..A.r \ _____ _ '"" If/ - 'f II: 3s )61' (..., 0 l rvvLC. (7":" 5/" ,J) . JI

II "(,0 t;k.d7/d ( P":! ifW'=-~"?T' " ;4S ~1.... h~1r-~ /'.' ,'Ii ,Jii vJ<Yf <-r ~ 0( B>lQft2 1"XYtSk:,

?o-<£.'':J '"'p tv;.w . -f/'I--=- '&llll~j),z:J df}-l-,e-: { JZ}J Y pc-; ~f 6~ . 10 1"1-'6/2-010

I ) 10 u1P5:k..) o...J ~~::.) o...c:.J. t ~ "'~f ) 0L.. ~ v-0~' I( It. J ....... c. .-'-'-'-&~

oS ~.k.e. I C';yr" '"'"7 ' ~~ cl- GO( /11'- ..J c,.. .(C~·. k.

, iJ-._~~.! , .: ..•. :-,-1- :::

. ~ ,'t:'. . I ~. ,. \ .. \

\ . i

. , \

I '_, <' . .

" " )'- .... ~ . . .

( . i j i ~ I! i. I

" . \ , II ." \ 1 , ' - , , '. , _. f

.- .

, \

•

. .

_. \~

, '

-- L

( I ~.<'

":1 ,~. ,

_-,Lt-~),-;:

·"~r ~ - .,{;. : 1.,,-' - , -"-J " '-:-' .'

. (

, '

- I . _

>, ( i . ,. .,

//~ ~ )

L . + -.. " .- ' \

;,\. !

"

f \

\

.. d

, <

. '

, I

: 2 -

' .

.. ' j

"

,

. , ,

"

-...J- / ' A..- __ v~ _/ ;/ :r1 ~b-'V"'" -:- /V' 0/Jt.~cA...~v .. '--_ ~_

( " ' " ' '-::>l..._ ~ 1;r.s7( tz.>lJ"'ll,0'J-.. ; .. ..-J lck.c.::.~b'--... Lol f6r- ~~,- ..

' I (;'11 ".", i " , ~(:-~Q,1 '.). /f'..-{J- .~ (.I. . ":"",, ~ y;"uJI!..-- N-t.-j ~L';)

JJ ,~, ~"L ~ ~,~ .... ->-- ~-';)rl.. .. _- J.j:~_ b 'fl-,af.---I Y.:.c W->-- )"';1

Attachment 2 Non-SCADA Data – Inspection Log Forms


FINAL



• CH2MHILL FAP ASTP Inspection Data Log Form -- COMPUTER CONTROL SCREEN READINGS

;

"". ""'" '_00 w •• , m~'" G'M

~ '"~" "" -- -"", ... ,- , ",.", "" ~-:r -p($SSU'e

'''~'"' '" ~~" "" i'r~ -

""""'" ,~ FIT';>1! G'M 0· 0 ' .... ,. PIT-.3131 '" ~;,~ ,,,,01 .

LX.;J13'- ----= FEET

"",, ' . "'~'" G'M

I~ ' ,,,.m '" ~;~~-" C-':' ~~m "" , "'~m oeM '1:? -"" "

"'". ," R" """ """, ,~" "" 0

'"'" "" '" i';': ..... ,.",

"" z· I ,~'"' "" l..',8'f?-.'I ,,- ,~" "" ~u.t..

TOl

',PO Equlpmont 10

:: fill:. ~!'f~'" Comments

FIT-3121

Discharge FIcH. FIT.J ' , ""- I" ,/. - - --

FIT.J131 ""- ~(" On. --

FIT.Jl32 "" , FIT-3133 "" , """. 1",-----

~ .. ,0 ,:,,:-"CAL R .. dI" Comm9nts - - -Z:::~:;i - "",~ "m "" ".,

I··· . .

"" ,~

I ' ~ ~ __

"" ,~

. . , II~~~J~~ ,

"" ""-

"" '" . . --

~tJ-.O I- .. . ,,,. "" '" #-,., "" 1·'<-

,~~ "" """'" I~o

"" '" , "" '" ",,4 . , ,,,,,,,- "" • 4'f7.

HEALTH AND SAFETY INSPECTION ,

",w"'" 1'= - cc .~

,~.

!Leaks or Med'IIri::8l ProbIern. Ob5&rVe<l

Initials of sampling personnel ~ O,,,mm, q / 2-'1/ 2''''0 I Z' I

Inspecloon Oata log Form_xis

• CH2MH ILL FAP ASTP Inspection Data Log Form - COMPUTER CONTROL SCREEN READINGS

",.- , .~"~:," ,,,""' " m~", "'" . 7_ i1

. ,'.H_ "'~ . "" .( ""',.., ... , '''~, "" "'= "'~. "' '" 'Z-n~" "'~" "IT I.q

m~" G>M

"'~." '" , "'~'" "" I 'l" m~", "'" " Z. '''~m '" ~. :1-"'~'" "" 00 , rn;;- m~", G'" .(.

1 .. ",- " '" " '. <;

eo'. " " '"' Comments ,~, ""

I" ''''' "" ~ ''''' "" ;;;;,; ,~'"' ~, ~'¥i '> .. ,,-,.'" "" , • so","

Equipment 1O Units FIT Y Reading Comments

m~", ""-

II , rn;;- m~" ""-, m~", ""-~ m~'" ""-.,-,-,~ m~m "" "'''" .. ....

I I

~ ~r-~ w' "., 1,-"", w' .~

1,-, , w' .~ :l r.'t w' ""- . 11'

I,,~ , ..... w' '" 0 1,,- , , ". W' '"

"" 1 •• 00 ,," It C;

"" 1 ~"'" (0

I "fi~ ."~,,.,~ WA '" ~

I',~. l d Water Bag Filter WA '" .l , WA , (,. HEALTH AND SAFETY INSPECTION

I ; I

" Eyewao.h ~ lout, dot) ~ ..

F '::'::'''':- Eyewash In'~ Ilns"")

IF~-E'l~ Inspect"" ---- -----

__ ~ _c ~_. OK

, "'- J -t -Initials 01 sampling personnel 'i4<7 ~ Oatem me cr~ ' / I'?:.HJ

I ~, ,

CH2MHILL - FAP ASTP Inspection Data Log Form

, 1 Tonk level

COMPUTER CONTROL SCREEN READINGS

~I~~~~

LX-311

FIT -311

PIT -3131

lX·3131

FIT·3131

PIT-3132

l)(·3132

FIT·3132

,~,

I~ ,~, P-361 HRS

Comm~nts

Comments

--

~

-

~ ~~

-

. ,;:;;. ~~~~~~~ I-~-,~~", "" . ~ fl'~=·~·'~==~~~-------Lrof.'~''''~~_oi,"C''A~L~~·~L-~--------~

. _.c

Insped"'" Data Log Form ....

Bag Filter

Equipment to Units

m,,,, m~'"

FIT-3131

m"~

HEALTH AND SAFETY INSPECTION

""""

Initials of sampling personnel _ _____ _

Comments

-

-

~ ~

C H2MHILL FAP ASTP Inspection Data Log Form -- COMPUTER CONTROL SCREEN READINGS , ""'" " "log Comments

m.,,, GeM -rti __ i-l • •• 1 PIT~91 FEET

LIT-3Jl -- FEET '-j·b .3 --,rr.", -,,, % .0 _

I '~"" w;; ,~, ~." ' m IIV,L -IPcnpO-og Wei Discharge FlOw FIT-311 G'M f~7: ~

, };~( PIT-3131 '" j r5 :0-~,,,, 'm -- - ----- - --

.. S' - ---- ----- - _. m.", GeM __ 4 ;:k -----------",.,~ '"

, Pres,,"

~tJ];'ft Level 1_ LX-3132 _ , m

",. FIT -3132 :;' , ... ,_ . __ ._--- l{.-", ~

,'K" ""'" ""'" Comments

IACid Feed Punp ,~, "" .~. 7}7 -; --

lAS SIrq:>e< B~ ''''' "" JO'iHD

~t' hI ------,

,_ 1'-381 "" --

'''''' 1'-3101 "" 1..,l~:lq I"""", w. ''''''

-P.Jll ~,

. ~" Equipment 10 Units FIT Y Reading Comments

>IT.", '? . ,...,. I 'J.1 ;8 ",31 I '~"'" I ,,~ m,,, ""-

~~1 "-- -

')~i I-I m.", ""- {~ .. -

. -,-,~ m.'~ ""- '7; . . " ... ,-, .... m.'", ""- "'''''' I"'''' , I Units ""'" Comments

[iiiiiiiii - !""" .'I,

-- --W. Ft") ~C:<j7b '. ::=-c . w. .~ i> "7 I w. .~ ,g -- --

. w. ""- , t 27f3 w • . '" .1-

. ,: - I~uent Bag F;~ --~. 1."2. __

. ---w. -p:~~

IAr S~ S"""er Ali';'" Rate '- . . ---._-w.

'~bba IA~ S\tIppef S...-np Pros,," W. "'"'0 w. '" ~~~ ic- C c ,--w. "'- el' ",..iI", "I. . - w • ,


" L---, '7 7'/

7

Initials 01 sampling personnel -,,1.- DatefTime (OI11/tt / '1 () ) J

CH2MHILL -

$ .... ,

Sngle l- I

Sngle I -

,

,.

"'. 1Ai' StrW« BlOwer AOfIow Rale

IAr S\Jl)per Scrnp Pre.,,",

aIIer Transter Pcmp



P-311 "" ,., Equlpmenl lD Units

, i>-H20

'"


, ,',.,",

Comments

-

Comments

--

Comments

Initials of sampling personnel ______ _ DatelTime \1 Ji '\ /7..DIO

1rtspec1."., Oata Log Form.xIs

CH2MHILL FAP ASTP Inspection Data Log Form - COMPUTER CONTROL SCREEN READINGS

,,,,,, "" ""'" R .. "" Comments

" .. ~, , m~'" Ge. y , .. -

-"':'" "" . -z: 7.-'1' -

.'''~,~. UT.331 m, 11 (,'/ ;= '" ,;e, '" --

"'~. ~,,, 'w .~}<' .. ~

o;scharQe Flow FIT';!1 1 G'. ,,, .. , PIT.;J131 '" 38;:' ~

~."" "" 1< .« -

m~'" G~ 1#. f' -

,rr,m '" 3# U'-, -

-, ~·'m "" -, FIT-313.2 _ GeM U"l'. ,

AA ," ~ ... """

" ,~t Roo ~;:::. "~"R""" Comments

""'-,~, ,~, "" •• , -':'" "" -" • .",q . • --

P-381 "" ZV.1fI1.f. ;;;;;;;;- "" 31

-P-3101

,~"" ~, ,~, ,.", "" Wc EQuipmenl 1O Units Comments

m~,,, Me

P4;:~? 'g3

i'~ .,~ m~" Me 11~ m~", Me . " 1\ ~(,

''"-'-'~ m~m Me < ,"-,-,~ '"~,~ Me '''''' .. I~-

~ "" ~'"~ --- w, .. , ''''' JlI' I ~ <f ,,-, w' . ''''' ~ :t.,. ;., Me In r .q.~\(

---, w, '" I '.1-~, F~&r W, '" 1..G

1M St~ Blower Airflow Ral. W, -

q.C 1Ai" Str«>er S..-np Pres ...... W, in-H20

~i after T ...... l'" Po..mp W, '" ".,-~ , w, '" .-w, .. ,.X;/.


t , .--,

--

""'""~

Initia ls of sampling personnel ~ ___ __ ~ OatefTime ItJ'a-4lul.

Inspection Data Log Form ~Is

• CH2MHILL FAP ASTP Inspection Data Log Form - COMPUTER CONTROL SCREEN READINGS

, ."~:'" --"""'- Comments

" ~ mo", oeM I"L~ ",.", "" ~~ .--- -IAcid Tn L_ ,,,.,,, "''- r.~, -"" ~"" '"

- - -

- '\I ' -- -

I '~..., .. '- ~"-- "" FIT-'Jl 1 G'. il --,~- PIT-3131 '" Le. eI _ ~o", "" ) --

,~ FIT-3131 G'. Jr--'" _.

PIT-31:l2

Well t.e.el ~.m " " o~,~ mom GO>. LJ..c.~

1 .. ",- AA .. .., .<,

""'a • "'"~" IAcid Feed Pump P-331 HRS 2--t : ,- ,~, "" I ~I!£r~_ I ,

,~, -"" ~1~!~t -":"" "" ~;&... ,." ""~

'v LOCAL I AY

Equipment 10 Units Comments

" m·,,,, G'" I i ~::; -,;'V.c . --, m., G'" I;¢.,,,",,;;'" . ,~ mo", "'" I ... - m"", "'" ~~~ 10;; ,~ mo,,, "'" I~'"

~ ~I::" CA~ w, "" . ;~

---

'" ,~ .; .V .-w, ,;;;;-

. " ", .. , . W, G"- 1'6'Z' ,D . w, '" _4:.J:"::, .. ,., .. w, '" ~-1 -w, 1"'00 '" W, in-H20 , "" , -w, '" C, , w, '" ~\7::'''' ,;';:,,'; . ..... ' w, • 1-


" o,~ ... ) ... .. -

, n (In500e)

'"-,00

,_ ... _ , /' Initials 01 sampling personnel ~ ~ o."mm. IzMIU/,7 filE_

";/ I Inspection Data log Fomuis

CH2MHILL -c.,1 ,_ J 'll J (.

~K-.J ~ , ."""-tY

(~J 1. xV-/'1,1.



"",. ~o ""'" ""'"' " "'M ~~. z. ,,_.- m ~" "" -~

~~ .. " .. ~ .. , LlT-3Jl FEET

,,,~.~ PIT-3101 -- '" ~

-em III.'{ ______ .~. LX-311

- ---- --Discharge Flow FIT-311 GeM ..... ,

~'1OCtoon Wei PM ........ PIT·3131 '" ,+'"2.. " ~ ~oon Wt>Y Level

- ---- -

~"'" m , 15'1'· ' ~

~; ~ion W"" Flow GeM II-Z.5 - -~

FIT-3131

c-' .. . 1__ PIT-3132 '" I ~!l--~ , LX-3132 FEET

FIT-3132 "'_M-:-

"" -~'- s-:,

,'''" "" """"" @ ~e __ n" "" ''''' '" ,I' J -

n" ""-'"'" --

",,- ,(,.J ,,~ n" "" "'yp' " Units Comments

, "'"'" ,,« 11q.jS, . . m~" G'" I J' ,1 " ,,, .. "'"'" GA. -

.e~ "'"'" GA. ..

.e~ "'"'" GA. "" .... I"'"

~ , U;,~"CAL R •• "", Comments

~ - ---->I" 't c\-

w, ,-w, ,- l iZ:

" .... , w, GAl. ~o W, '" ,.;

,,~ >0. W, -'" 'Z.'-I w, 'i-! w, n->W ,(: 0 w, '" ') .. -w, '" LKJ ••

- --, , .- w, , /#.\;7.


" - "'~.~'

(Inside)

l eaks ~ Problems OboeNed ---

Initials of sampling personnel OatelTlme IZ/Z."t /z.,a t-Inspeclion Data log Form., 1s

Attachment 3 COC Recovery Calculations


FINAL



Reporting Period Date

Extraction Well Totalizer

(gal)Begin September 24, 2010 140,526,910Mid October 29, 2010 144,449,995Mid November 26, 2010 147,928,979End December 24, 2010 151,253,870

Sample Location Sample ID Sample Date TCE cDCE tDCE UnitsInfluent water FAP SP-1 12/14/2010 5.7 2.3 0.66 µg/LEffluent water FAP SP-5 12/14/2010 0.25 0.25 0.25 µg/L

Effluent concentrations are the detected concentration or 1/2 of the MDL which ever is greater.

cDCE tDCECI = 5.7 µg/L = Average Concentration in SP-1 (influent) Water Sample 2.30 0.66

CE = 0.25 µg/L = Average Concentration in SP-5 (Effluent) Water Sample 0.25 0.25DC = 5.45 µg/L = Concentration Removed 2.05 0.41

V2 = 144,449,995 Gallons = Final Extraction Well Totalizer ReadingV1 = 140,526,910 Gallons = Initial Extraction Well Totalizer Reading

DV = 3,923,085 Gallons = Volume of Ground Water TreatedDV = 1.49E+07 Liters = Volume of Ground Water Treated this Period 1.49E+07 1.49E+07

M (mass) = DC * DV * ( 10-9 kg/µg)= 5.5 µg/L * 14.85x10^6 Liters * 10-9 kg/ug

M (mass) = 0.081 Kilograms = Mass of Contaminant Removed from Ground Water this Period 0.030 0.0061




DV = 3.48E+06 Gallons = Volume of Ground Water TreatedDV = 1.32E+07 Liters = Volume of Ground Water Treated this Period 1.32E+07 1.32E+07

M (mass) = DC * DV * ( 10-9 kg/µg)= 5.5 µg/L * 13.17x10^6 Liters * 10-9 kg/µg





DV = 3.32E+06 Gallons = Volume of Ground Water TreatedDV = 1.26E+07 Liters = Volume of Ground Water Treated this Period 1.26E+07 1.26E+07

M (mass) = DC * DV * ( 10-9 kg/µg)= 5.5 µg/L * 12.59x10^6 Liters * 10-9 kg/µg


Effective COC Recovery Calculation (Based on Water Concentration)Trichloroethene

Effective COC Recovery Calculation (Based on Water Concentration)Trichloroethene

October 29, 2010 to November 26, 2010Effective COC Recovery Calculation (Based on Water Concentration)

Trichloroethene

November 26, 2010 to December 24, 2010

ATTACHMENT 3COC Recovery CalculationsFruit Avenue Plume Superfund Site - Air Stripper Treatment Plant, Albuquerque, New Mexico(September 24, 2010 to December 24, 2010)

Fundamental Values Data Table

September 24, 2010 to October 29, 2010



FINAL



Attachment 4 Response to Comments on the draft CSR No.


FINAL



RESPONSE TO COMMENTS FRUIT AVENUE PLUME SUPERFUND SITE

CSR NO. 30, DRAFT

FAP_CLEANUP STATUS REPORT NO 30 1 OF 1 FEBRUARY 2011 ES021411044224DFW\110450047

Task Order: 0003-RALR-06DD Project: Fruit Avenue Plume Superfund Site Albuquerque, New Mexico Document Title: CSR No. 30, Draft Submission Date: January 2011 EPA Comments (no comments)

1.

NMED Comments

Item Section Page Comment Explanation and Response

1. Page 7 Abbreviations and Acronyms

RAO - remedial action objective instead of remediation action objective

The definition for RAO will be changed to “remedial action objective”.

2.

3.

ABCWUA Comments (no comments)

Item Section Page Comment Explanation and Response

1.

2.


FINAL



cleanup status report no. 30 - period of september 24 … · cleanup status report no. 30 –...

Documents