Monthly Cleanup Status Report – No. 13 Period of October ... · CLEANUP STATUS REPORT 13 –...

$: Monthly Cleanup Status Report – No. 13 Period of October ... · CLEANUP STATUS REPORT 13 – NOVEMBER/DECEMBER 2006 VERSION 1.0 345406\T10\FAP_CSR_13_2006-12.DOC 3 DECEMBER 2006$
345406\T10FAP_CSR_13_2006-12.DOC 1 DECEMBER 2006

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

Monthly Cleanup Status Report – No. 13 Period of October 16, 2006 to December 15, 2006 Fruit Avenue Plume Superfund Site PREPARED FOR: Bartolome Cañellas/EPA

Sabino Rivera/NMED Eileen Shannon/CoA

PREPARED BY: CH2M HILL COPY TO: William LeFevre/CH2M HILL, Albuquerque

Jeff Gamlin/CH2M HILL, Albuquerque Kevin Bral/CH2M HILL, Denver Mike Brewer/CH2M HILL, Albuquerque John Knott/CH2M HILL, Dallas Amy Halloran/CH2M HILL, Albuquerque Peter van Noort/CH2M HILL, Dallas-Fort Worth

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

DCN 0003-02012 DATE: December 22, 2006

1.0 Introduction This bi-monthly cleanup status report (CSR) summarizes operation 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 (FAP) Superfund Site (CERCLIS No. NMD986668911) located

in Albuquerque, New Mexico. While previous reports have been published monthly, this and future

reports will be published every two months. This report describes O&M activities performed on the

system from October 16, 2006 through December 15, 2006.

The FAP Superfund Site (Site) is identified on the National Priorities List (NPL) as a chlorinated

solvent ground water plume located in the downtown area of Albuquerque, New Mexico. The

primary contaminant of concern (COC) in the ground water at the Site is trichloroethene (TCE) with

lesser amounts of tetrachloroethene (PCE), cis-1,2-dichloroethene (DCE), and trans-1,2-DCE. A

treatment system was constructed between August 2004 and September 2005. Routine operations of

the system started on November 18, 2005. A summary of startup operations may be found in Cleanup

Status Report No. 1 (CH2M HILL, 2006). Although some modifications to the treatment system

FRUIT AVENUE PLUME SUPERFUND SITE CLEANUP STATUS REPORT 13 – NOVEMBER/DECEMBER 2006

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have been initiated during this reporting period, for the purposes of this report the system consists of

one ground water extraction well (D2E-P1), two injection wells (D2E-I3 and I2/D1E-I1) that contain

a total of three screened intervals for re-injection of treated water into the aquifer (single injection

well [D2 aquifer zone], dual injection well upper tube [I2 aquifer zone], and dual injection well lower

tube [D1 aquifer zone]), and an air stripper treatment system. The treatment system location is shown

in Figure 1; the layout of the system is provided in Figure 2.

The FAP Superfund Site Record of Decision (EPA, 2001) established a remediation action objective

(RAO) for operation of the treatment system that prevents human ingestion of, inhalation of, or

dermal contact with ground water that contains concentrations of PCE above 5 micrograms per liter

(µg/L), TCE above 5 µg/L, DCE above 70 µg/L, and trans-1,2-DCE above 100 µg/L (these are the

Maximum Contaminant Level Goals [MCLGs] set by the Clean Water Act (or are MCLs where

MCLGs are set at zero)).

To meet this RAO and Applicable or Relevant and Appropriate Requirements (ARARs), the

treatment system has the following operational goals:

• COCs at concentrations less than MCLs at the ASTP effluent,

• Air emissions below state and federal threshold levels,

• Maintain >80% run time, and

• Maintain contaminant plume capture.

2.0 Operations Summary This section summarizes the field activities and presents the operational data that were collected from

the treatment system during the 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. The performance of

the treatment system was monitored by onsite staff, and by remote monitoring of the SCADA system.

A list of ASTP operational parameters monitored is included in Table 3. Onsite observations of non-

SCADA operational parameters were recorded on inspection data log forms. Data from the

inspection data log forms for system monitoring and operational activities through this reporting

period are reported in Table 4. Field notes documenting field activities are included in

Attachment A.

Modifications to the ASTP continued during the reporting period. The dual injection well

redevelopment and reconfiguration were completed and the dual injection well was brought back on


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line on October 21, 2006. The single injection well was shut down on October 23, 2006 and

redevelopment began on that well. The ASTP was shut down on November 20, 2006 to install a new

reinjection pump and work on the extraction well (which also requires the ASTP to be shut down)

began on December 7, 2006. As of the end of the reporting period, the ASTP is still shut down to

allow the system modifications.

2.1 System Downtime The goal of exceeding 80% run time was not achieved during this reporting period. The treatment

plant was operational 827 hours of a possible 1440 hours, or 57.4% of the reporting period. Except

for the down time for system modifications, the ASTP would have been operational for 99% of the

reporting period. The ASTP runtime calculation and history are presented in Table 5.

Downtime during this reporting period that was related to the recent system modifications occurred

during a short-term draining of well vault piping and for the installation of the new reinjection pump.

Details of these events are included below in Section 2.4.1. Downtime during this reporting period

that was related to normal operations and maintenance occurred while changing the bag filters and

injection well back flushing and only resulted in minimal impact to the overall run time. The

following list summarizes the routine system shutdown occurrences and durations during this period.

• The system was shut down at 10:30 on October 19, 2006 for back flushing and a routine bag filter

change and restarted at 16:08. Downtime attributed to this reporting period: 5.63 hours.

• The system was shut down at 10:00 on October 23, 2006 to drain pipelines for the single well

vault demolition and restarted at 11:45. Downtime attributed to this reporting period: 1.75 hours.

• The system was shut down at 11:45 on October 23, 2006 for a routine bag filter change and

restarted at 12:30. Downtime attributed to this reporting period: 0.75 hours.

• The system was shut down at 11:10 on November 17, 2006 for a routine bag filter change and

restarted at 12:02. Downtime attributed to this reporting period: 0.87 hours.

• The system was shut down at 11:20 on November 20, 2006 to install a new reinjection pump and

to continue modification work on the extraction well. The system was not restarted before the end

of the reporting period at 12:00 on December 15, 2006. Downtime attributed to this reporting

period: 604 hours.


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2.2 Operational Data and Process Monitoring Data The ASTP SCADA system continuously monitors the operational data listed in Table 3. Non-

SCADA parameters are monitored approximately once per week. Figure 2 illustrates the locations of

the water and exhaust sampling ports, SCADA monitoring instruments, and the location on non-

SCADA instruments. The data recorded by the SCADA system is saved on a hard drive associated

with the computer system. The hard drive is backed up monthly. The non-SCADA data recorded by

the operator on the inspection data log forms are included in Attachment B. Field notes

documenting field activities are included in Attachment A.

2.2.1 Plant Influent and Effluent, and Efficiency of Aboveground Treatment Components A review of the trended SCADA data indicates that the ASTP operated at a total injection rate from

40 gpm to 86 gpm with an average of 53 gpm during this reporting period. The total injection rate

has currently been reduced from the initial startup rate of approximately 85 gpm because reinjection

was generally limited to only one injection well at a time while the other well was being redeveloped

and reconfigured.

The cumulative and monthly volumes of ground water extracted and injected by the ASTP are

presented in Table 6 and Figure 3. The total flow data for November 17, 2006 is used for the end of

the reporting period because after the ASTP shut down on November 20, 2006 the SCADA system

was shut down before a total flow reading could be recorded. This flow reading will be collected

when the ASTP SCADA system is restarted and the flow quantity will be added to the next reporting

period. It is estimated that approximately 170,000 gallons will be shifted from this reporting period

to the next.

Through the end of this reporting period, a cumulative total of approximately 39,600,000 gallons of

water have been pumped from the extraction well and treated by the air stripper, approximately

37,900,000 gallons of treated water have been re-injected via the injection well system, and

approximately 939,000 gallons of treated water have been discharged to the sanitary sewer. During

this reporting period, approximately 2,310,000 gallons of water have been pumped from the

extraction well, treated by the air striper, and re-injected via the injection well system and no water

has been discharged to the sanitary sewer.

Historical COC concentrations in the ASTP influent (sample port SP-1) and effluent (sample port SP-

5) are summarized in Table 7. As the MAROS Mann-Kendall evaluation conducted for the

September 2006 CSR indicates that TCE concentrations are stable, and due to scheduling difficulties

associated with plant down time, it was determined that the current months performance could be


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adequately estimated using the previous month’s analytical sampling results and so samples were not

collected during this reporting period.

The mass removal of COCs by the treatment system during this reporting period was estimated based

on the total volume of ground water pumped from the extraction well during the reporting period and

the difference between the influent and treated (effluent) water concentrations as measured during the

October 16, 2006 sampling event. A concentration of one-half the detection limit (0.25 μg/L during

this reporting period) was used if a particular COC was not detected in the treated water sample.

Calculations of the contaminant mass removed by the system are illustrated in Attachment C. The

cumulative and monthly mass of COCs removed from ground water since the treatment system

commenced operations are presented in Table 8 and illustrated in Figure 4. Approximately 2.71

kilograms (kg) of VOCs (consisting of TCE, cis-1,2-DCE, and trans-1,2-DCE) are estimated to have

been removed from the ground water aquifer since the treatment system began operation. PCE has

not been detected in the influent water samples.

All previously collected air emissions samples have shown that concentrations and emissions were

below applicable regulatory standards. Since the influent concentrations of VOCs in ground water

have not varied appreciably since startup, the concentrations observed in the air emissions are not

expected to have appreciably changed. Therefore, an air emissions sample was not collected during

this reporting period.

2.2.2 Extraction Well Data A review of the trended SCADA data indicates that the pumping rate for the extraction well (D2E-P1)

ranged from 92 to 108 gpm throughout this reporting period. The extraction well pump is cycled

on/off to maintain flow balance with the re-injection system. Flow at the extraction well is manually

controlled through the SCADA system to maintain a fixed flow rate so that the frequency of on/off

cycles is minimized. A comparison of the extraction well and injection pump timers shows that the

extraction pump operated approximately 51% of the time during this period.

It is assumed that the conclusions of the capture zone evaluation are no longer applicable because the

extraction well operated at approximately 60% of the flow rate and operational runtime that were

included in the capture zone evaluation in the March 2006 CSR. The original conclusion was that the

vertical and horizontal extent of the capture zone is as was expected when the location of the

extraction well was selected, which were as follows:

• Little or no capture is occurring in the I2 zone. The extraction well is screened across the D2

zone only and does not appear to be affecting the I2 zone.


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• In the D1 zone, capture of contaminants identified by the monitor well SFMW-22 appears

successful. Contaminants downstream and south of the pumping well are not being captured.

• In the D2 zone, capture of contaminants identified by the monitor well SFMW-23 appears

successful. Contaminants downstream and south of the pumping well are not being captured.

Contaminants upstream of the pumping well will likely not be captured as they would tend to

move around the injection boundary.

Because operation during this reporting period was limited due to well redevelopment and

reconfiguration activities, the groundwater contaminant capture zone during this period was limited

and likely less than previously estimated. Since this is a temporarily limited operating condition, no

further analysis was conducted to define the limitation of capture. Upon completion of the well

reconstruction activities, the capture zone will be re-assessed and will likely be equal to or exceed that

previously estimated.

2.2.3 Injection Well Data During this reporting period, redevelopment and reconfiguration of the dual well were completed and

it was returned to service on October 21, 2006. After the modifications to the dual well, it retained its

two screened intervals but they are not independently controlled. Injection to the single injection well

was stopped a few days later on October 23, 2006 to allow redevelopment and reconfiguration of that

well. Work on the single well was not completed by the end of the reporting period.

The flow of treated water to the injection wells is manually controlled through the SCADA system to

maintain a fixed flow rate at each injection well. The FCVs are programmed to stop injection when

the water in the well reaches a predetermined level. The injection FCVs are programmed to maintain

water levels below 20 feet below ground surface and achieve the following approximate flows:

• 50 gpm to the single injection well (D2E-I3) while in service as discussed in Section 2.4.2.

• 45 gpm to the dual injection well (I2/D1E-I1) while in service as discussed in Section 2.4.2.

The specific capacity of each injection well was calculated from data collected before and after

redevelopment. As expected, the specific capacity of the single injection well increased from a pre-

redevelopment capacity of 3.1 gpm/ft, to a post-redevelopment capacity of 3.4 gpm/ft and the specific

capacity of the dual injection well increased from a pre-redevelopment capacity of 4.0 gpm/ft, to a

post-redevelopment capacity of 4.4 gpm/ft.


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2.3 Problems Encountered With P&T Component Operation On several occasions over the past months, leaks have been discovered in the carbon steel process

piping and have been repaired. Additionally, injection well capacity and pump efficiencies have

declined more and faster than expected. Trouble shooting and process- and infrastructure-design

modification efforts continue in response to these leaks and are or will be documented in separate

technical memos.

The ASTP had been running well for most of the reporting period. Problems encountered are

concerned with the system modifications. Except for the down time for system modifications, the

ASTP would have been operational for 99% of the reporting period.

2.4 System Modifications, Maintenance, and Testing The purpose of this section is to summarize routine and non-routine maintenance and system

modifications performed during this reporting period and to identify maintenance activities scheduled

for the next reporting period.

2.4.1 Routine Maintenance As part of the routine maintenance procedures for the treatment system, each injection well is

backflushed. To ensure adequate staffing and equipment availability, routine backflushing is

generally conducted by a subcontractor every two weeks. A detailed description of backflushing

operations is included in the March 2006 CSR No. 5. Injection to a well is suspended while it is

being backflushed and restarted as soon as work is complete. During this reporting period, the dual

injection well was not backflushed because it was out of service for rehabilitation and because the

well services subcontractor was busy working on the single injection well. The single injection well

was backflushed on October 19, 2006. Additional backflushing is scheduled for the next reporting

period.

Additional routine maintenance performed during this reporting period included changing the bag

filters. Changing the bag filters requires that the ASTP be shut down long enough to drain the filter

canisters. The effluent filter bags (BF#2) were changed on October 23, 2006. Both the influent

(BF#1) and effluent filter bags (BF#2) were changed on November 17, 2006.

The air stripper view windows have remained generally clear and pressure in the air stripper has

remained within acceptable limits. Some orange buildup is visible on the view windows and there is

a slight buildup of deposits on the trays. The air holes in the trays are not blocked however so


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cleaning of the air stripper trays was therefore not conducted during this reporting period. Tray

cleaning is being considered in conjunction with the system

A sulfuric acid delivery was received on October 26, 2006. Deliveries have been less frequent than

usual because the treatment plant has not been running at full capacity.

2.4.2 System Modifications and Non-Routine Maintenance On November 20 to 22, 2006, a new reinjection pump was installed. The new pump (Vanton Chem

Guard CGA/ANSI 3x2x6), is made of acid resistant materials. O&M procedures for the new pump

will be added to the O&M Manual. Piping modifications to accommodate the new pump are being

made and the pump will be started in January 2007.

Well vault piping at the injections wells has been replaced with acid-resistant materials by the

plumbing subcontractor. Work on the pumping well will begin as soon as the well-maintenance work

is done.

Throughout the reporting period, the well-maintenance subcontractor worked to redevelop and

reconfigure the wells. Nearly all work is complete on the injection wells and work continues on the

pumping well. Tasks completed by the well-maintenance subcontractor include pre- and post-

redevelopment down-hole video inspection of the wells, swabbing, bailing, airlifting, and jetting of

the wells, and reconstruction of the down-hole components. Work on the injection wells was

completed by December 7, 2006 when work began on the pumping well.

2.4.3 Corrosion and Process Chemistry Testing In response to the recurring pipe leaks and FCV failure, trouble shooting, and process- and

infrastructure-design modification and reconstruction efforts continue. The system modifications will

be presented in a separate design report.

3.0 Conclusions The ASTP was functional during this reporting period. Based on the monitoring and observations

made during this reporting period, the following conclusions were developed:

• An estimated 0.15 kg of total VOCs (consisting of TCE, cis-1,2-DCE, and trans-1,2-DCE) were

removed from the D2 zone of the ground water aquifer during this reporting period.

• The treatment system was in operation for about 57 percent of the reporting period (October

16, 2006 to December 15, 2006).


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• Approximately 2.3 million gallons of water were pumped from the D2 aquifer and treated. All of

this water was re-injected via the injection wells.

• No water was discharged to the sanitary sewer.

• Previously measured air emissions were below state and federal threshold levels. As the air

emissions depend directly upon the COC concentrations in the influent ground water, and these

concentrations have not changed, it is assumed that the system still meets the goal of keeping air

emissions below state and federal levels.

• Infrastructure and process design modifications are being implemented in response to corrosion

induced leaks.

• Redevelopment and reconfiguration of the injection wells is complete. Work on the pumping

well has begun and is expected to be compete during the next reporting period.

• Installation of a replacement reinjection pump is nearly complete.

4.0 Recommendations/Upcoming Activities Influent and effluent water sampling, injection well back flushing, and acid deliveries will continue

during the December-February operation period.

Redevelopment and reconfiguration of the pumping well will continue during the next reporting

period.

Replacement of the vault piping with acid resistant materials will continue during the next reporting

period.

5.0 References CH2M HILL, 2004 Fruit Avenue Plume Superfund Site Remedial Action: Interim System

Evaluation. February 17 2004[DCN 04-5995]

CH2M HILL, 2006. Cleanup Status Report No. 1 – Startup Version 1.0. Fruit Avenue Plume

Superfund Site. Albuquerque, New Mexico. January 2006.

U.S. Environmental Protection Agency (EPA), 2001. Record of Decision. Fruit Avenue Plume Site.

Albuquerque, New Mexico (CERCLIS # NMD986668911). September 2001.


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Tables


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345406\T10\FAP_CSR_13_2006-12.DOC DECEMBER 2006


Table 1ASTP Operational Highlights (October 16 to December 15, 2006)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Reporting Period Start Date 10/16/06 12:00 PMReporting Period End Date 12/15/06 12:00 PMASTP operation time [hrs] 827Total volume [gal] of gw pumped during the reporting period 2.31E+06Total volume [gal] of gw injected during the reporting period 2.31E+06Total mass [kg] of TCE and other VOCs removedduring the reporting period 0.15Total mass [lbs] of TCE and other VOCs removedduring the reporting period 0.33Percent operational during the reporting period 57%

DFW\P\345406\T10\CSR_13\Table1-Highlights PAGE 1 OF 8 December 2006

Albuquerque, New Mexico

Date ActivityOctober 16, 2006 Reporting period begins at 12:00

Dual injection well rehab continues.October 18, 2006 Dual injection well rehab and reconfiguration complete.October 19, 2006 Routine back flushing of single injection well. Dual well does not need back flushing.

ASTP shut down from 10:30 to 16:08 while Single is back flushed.pH sensor moved from EQ tank to in-line location immediately downstream of transfer pump.

October 20, 2006 PIT, FIT, FCV actuator reconected and testedOctober 21, 2006 Acid dose modified to 387/70

Dual injection well on line at 15:45 (Injection to single well continues).Extraction well flow reduced to about 95 gpm to keep up with transfer pump.

October 23, 2006 Single injection well shut down at 09:00 for well rehab, injection to dual well continues.ASTP shut down from 10:00 to 11:45 to drain pipelines for single well vault pipe demolition.Effluent bag filters changed from 11:45 to 12:30.Acid dose modified to 387/65

October 26, 2006 Receive sulfuric acid delivery.October 27, 2006 Acid dose modified to 380/65.October 30, 2006 Acid dose modified to 385/60.November 1, 2006 Total Services Company (TSC) excavates pipelines under dual and pumping well vaults.

Redevelopment of single well by Hydro Geologic Services (HGS) continues.November 17, 2006 Influent and effluent bag filters changed, ASTP down from 11:10 to 12:02.

Reporting period ends at 12:02November 20, 2006 ASTP shut down (08:00) to install new reinjection pump, new piping in well vaults, and rebuild down-

hole componants of injection and extraction wells.

December 7, 2006 Work on extraction well begins.

December 15, 2006 ASTP still down for well and piping rebuild.Reporting period ends at 12:02

Notes:

bgs below ground surface

VOC volatile organic compound

gal gallon

ft feet

Acid Dose 403/63 Acid metering pump is set to start up at 63% pump speed went well pump starts then change to 403

μm micrometermL milliliterpsi pounds per square inch

FCV flow control valve

Table 2ASTP O&M Activities (October 16 to December 15, 2006)Fruit Avenue Plume Superfund Site

ASTP Air Stripper Treatment Plant

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Table 3List of ASTP Operational Parameters MonitoredFruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Trended Parameters - SCADA parametersFlow rates at each extraction and injection well head and the total injection flow (5 locations)Water levels in each extraction and injection well and the equalization tank (5 locations)Pressure at each injection well head and the reinjection pump (4 locations)Valve position for FCVs at each extraction and injection well (4 valves)Blower air discharge rate (SCFM)Blower discharge pressure (inches of water)Blower airflow rate (scfm)pH in the equalization tankAcid pump speed (% of maximum rate)Acid level in the acid storage tankAcid dosage factor set pointNon-Trended Parameters - SCADA parametersExtraction well hours of operation (hours)Injection pump hours of operation (hours)Air stripper blower hours of operation (hours)Acid pump hours of operation (hours)Transfer pump hours of operation (hours)Extraction well flow totalizer (gallons)Treated water injection total volume injected (gallons)Treated water injection gallons injected to single screen (gallons)Treated water injection gallons injected to upper screen (gallons)Treated water injection gallons injected to lower screen (gallons)Non-Trended / Non-SCADA parametersInfluent water pressure (psi)Post pre-treatment bag-filter water pressure (psi)Post transfer pump water pressure (psi)Post post-treatment bag filter water pressure (psi)Sanitary sewer flow rate and totalizer (gallons)Retreatment loop flow rate and totalizer (gallons)Potable water totalizer (gallons)

DFW\P\345406\T10\CSR_13\Table3-SCADAList PAGE 3 OF 8 December 2006

Table 4ASTP Operational Data (October 16 to December 15, 2006)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

FAP ASTP Inspection Data Log Form10/16/06 12:00 10/19/06 11:00 10/21/06 18:45 10/30/06 15:25 11/7/06 17:01 11/10/06 12:00 11/17/06 10:00 12/15/06 12:00

COMPUTER CONTROL SCREEN READINGSOverview ScreenTreated Water (Injection Well) Flow FIT-3121 GPM 51.4 54.3 86.1 45.6 45.6 44.4 39.7 0.0Equalization Tank Level PIT-391 FEET 3.53 2.27 1.46 2.78 2.34 2.12 2.84 0Acid Tank Level LIT331 FEET 2.78 2.56 2.43 5.28 4.84 4.7 4.32 NA - - -Reinjection Pump Pressure PIT-3101 PSI 51.0 50.4 42.2 51.9 51.8 51.9 52.8 0.0 - - -Pumping Well Level LX-311 FEET 101.6 101.3 104.3 105.9 106.7 108.5 108.2 NA - - -Pumping Well Discharge Flow FIT-311 GPM 107.1 108.2 93.6 92.6 91.9 92.4 93.0 0 - - -Single Injection Well Pressure PIT-3131 PSI 51.8 49.6 37.2 NA NA NA NA 0.0 - - -Single Injection Well Level LX-3131 FEET 166.6 156.7 156.9 NA NA NA NA NA - - -Single Injection Well Flow FIT-3131 GPM 51.6 52.4 46.3 0.0 0.0 0.0 0.0 0.0 - - -Dual Injection Well Upper Tube Pressure PIT-3132 PSI - - - - - - - - - - - - - - - - - - - - - - - - - - -Dual Injection Well Upper Tube Level LX-3132 FEET - - - - - - - - - - - - - - - - - - - - - - - - - - -Dual Injection Well Upper Tube Flow FIT-3132 GPM - - - - - - - - - - - - - - - - - - - - - - - - - - -Dual Injection Well Lower Tube Pressure PIT-3133 PSI NA NA 38.0 53.3 52.3 50.4 37.6 0.0 - - -Dual Injection Well Lower Tube Level LX-3133 FEET NA NA 68.2 71.7 73.5 74.4 73.9 NA - - -Dual Injection Well Lower Tube Flow FIT-3133 GPM 0.0 0.0 41.4 47.5 47.0 46.4 41.2 0.0 - - -Acid Dosage Factor Set point N/A mg/L 380/75 380/75 387/70 385/60 383/55 383/55 383/55 NA - - -Equipment Run Times ScreenAcid Feed Pump P-331 HRS 6,105.7 6,137.1 6,161.1 6,281.3 6,377.6 6,411.0 6,490.1 6,490.1 - - -Air Stripper Blower P-361 HRS 8,409.2 8,476.6 8,525.3 8,736.5 8,930.2 8,997.2 9,162.9 9,162.9 - - -Transfer Pump P-381 HRS 6,614.5 6,655.5 6,686.4 6,817.9 6,924.9 6,962.1 7,049.8 7,049.8 - - -Reinjection Pump P-3101 HRS 8,325.3 8,392.6 8,441.3 8,552.4 8,846.1 8,913.1 9,078.8 9,078.8 - - -Pumping Well Pump P-311 HRS 6,306.5 6,337.8 6,361.7 6,481.3 6,577.0 6,610.2 6,688.8 6,688.8 - - -Totalizers ScreenTreated Water (Injection Well) Flow FIT-3121 GAL 35,861,299 36,071,014 36,280,730 36,909,875 37,329,306 37,539,021 37,948,736 37,948,736 - - -Pumping Well Flow FIT-311 GAL 37,329,306 37,539,021 37,748,736 38,377,882 39,007,027 39,216,742 39,636,173 39,636,173 - - -Single Injection Well Discharge Flow FIT-3131 GAL 22,754,099 22,963,814 23,068,672 23,278,387 23,278,387 23,278,387 23,278,387 23,278,387 - - -Dual Injection Well Upper Tube Flow FIT-3132 GAL 3,722,445 3,722,445 3,722,445 3,722,445 3,722,445 3,722,445 3,722,445 3,722,445 - - -Dual Injection Well Lower Tube Flow FIT-3133 GAL 9,646,899 9,646,899 9,646,899 10,276,045 10,800,333 11,010,048 11,481,907 11,481,907 - - -LOCAL EQUIPMENT READINGSSanitary Sewer Utility Meter - Outside ASTP N/A GAL 939,097 939,097 939,097 939,097 939,097 939,097 939,097 939,097 - - -Water Utility Meter - Outside ASTP N/A Ft^3 544.64 544.64 544.64 544.64 544.64 544.64 544.64 544.64 - - -Electric Utility Meter - Outside ASTP N/A kWh 42,341 42,194 - - - - - - - - - 49,577 51553.8 - - - - - -Electric Utility Meter - D2EI3/D2EP1 N/A kWh 67,191 67,525.5 - - - - - - - - - 70,353 - - - - - - - - -Recirculation Totalizer Inside ASTP N/A GAL 1,009,832 1,009,832 1,009,832 1,009,832 1,009,832 1,009,832 1,009,832 1,009,832 - - -Pressure Gauge at ASTP Influent N/A PSI 6.0 5.0 6.0 6.0 6.0 6.0 6.0 0.0 - - -Pressure Gauge after Influent Bag Filter N/A PSI 3 2.6 2.5 2.8 2.8 2.5 2.4 0.0 - - -Air Stripper Blower Airflow Rate N/A x100 CFM 9 9.1 9.1 9.1 9.1 9.5 9.2 0.0 - - -Air Stripper Sump Pressure N/A in-H2O 14 14 13 14 15 15 14 0 - - -Pressure Gauge after Transfer Pump N/A PSI 0 0 0 0 0 0 0 0 - - -Pressure Gauge after Treated Water Bag Filter N/A PSI 50 45 36.5 52.5 52.0 49.6 37.0 0.0 - - -ACID Feed Pump Reading N/A Pulses 129 132 115 111 108 113 112 0 - - -ACID Feed Pump Reading N/A Stroke 83% 84% 84% 84% 84% 83% 83% 0% - - -Notes:ASTP Air Stripper Treatment Plantbgs below ground surfaceft feethrs hoursmg/L milligrams per literkWh kilowatt hourgal gallonμm micrometermL milliliterpsi pounds per square inch

Date & Time

Data after the ASTP shutdown on 11/20/06 are not available because the SCADA system is shut down. Total flow between Nov 17 and November 20 will be reported in the next CSR.

Acid Dosage Factor Setpoint 403/63 (e.g.) Acid metering pump is set to start up at 63% pump speed went well pump starts then change to 403 mg/L as pumping rate stabilizes.

The Dual Injection Well Upper Tube has been retired during the recent modifications. Pressures, levels, and flows are not recorded during repairs and modifications.

Equipment ID

Date & TimeDate & TimeUnits

DFW\P\345406\T10\CSR_13\Table4-InspectionLogData PAGE 4 OF 8 December 2006

Table 5ASTP Run Time Calculation and History (October 16 to December 15, 2006)Fruit Avenue Plume Superfund SiteAlbuquerque, New Mexico

Event Date/Times Event Date/Times Cause Reporting Date % OperationalStart 10/16/06 12:00 ASTP stop 10/19/2006 10:30 12/15/2006 57%Stop 12/15/06 12:00 restart 10/19/2006 16:08 10/16/2006 64%Reporting Period [days] 60.0 downtime [hrs] 5.63 09/15/2006 99%Reporting Period [hrs] 1440.00 08/15/2006 100%System Downtime [hrs] 613.00 ASTP stop 10/23/2006 10:00 07/18/2006 73%Operational Period [hrs] 827.00 restart 10/23/2006 11:45 06/15/2006 97%Percent Operational 57.4% downtime [hrs] 1.75 05/15/2006 99%

04/17/2006 98%ASTP stop 10/23/2006 11:45 Bag filter change 03/15/2006 85%restart 10/23/2006 12:30 02/15/2006 97%downtime [hrs] 0.75 01/16/2006 75%

12/15/2005 72%ASTP stop 11/17/2006 11:10 Bag filter changerestart 11/17/2006 12:02downtime [hrs] 0.87

ASTP stop 11/20/2006 8:00 Well and piping rebuildrestart 12/15/2006 12:00downtime [hrs] 604.00

Runtime History

Back flushing and bag filter change

Reporting Period Reporting Period Downtime

Drain pipelines for single well vault pipe demolition

hrsTotal Routine Downtime

613.00

DFW\P\345406\T10\CSR_13\Table5-RunTime PAGE 5 OF 8 December 2006

Table 6Volume of Water Extracted and InjectedFruit Avenue Plume Superfund Site Albuquerque, New Mexico

Cumulative Extraction

Cumulative Discharge

Monthly Extraction

Monthly Discharge

Extraction Well Flow(gal)

Treated Water Flow(gal)

Single Injection Well Flow

(gal)

Dual Injection Well Upper Flow

(gal)

Dual Injection Well Lower

Flow(gal)

Sanitary Sewer Flow(gal)

Extraction Well Flow

(gal)

Treated Water Flow(gal)

Single Injection Well Flow

(gal)

Dual Injection Well Upper

Flow(gal)

Dual Injection Well Lower Flow

(gal)

Sanitary Sewer Flow

(gal)

01/04/2005 - - - - - - 02/01/2005 172,001 73,539 30,575 13,169 14,762 113,495 172,001 73,539 30,575 13,169 14,762 113,495 03/01/2005 871,629 779,878 484,966 75,776 204,800 113,495 699,628 706,339 454,391 62,607 190,038 -04/01/2005 1,127,219 891,290 534,118 91,341 252,314 256,910 255,590 111,412 49,152 15,565 47,514 143,415 05/01/2005 1,127,219 891,290 534,118 91,341 252,314 256,910 - - - - - -06/01/2005 1,127,219 891,290 534,118 91,341 252,314 256,910 - - - - - -07/01/2005 1,127,219 891,290 534,118 91,341 252,314 256,910 - - - - - -08/01/2005 1,127,219 891,290 534,118 91,341 252,314 256,910 - - - - - -09/15/2005 1,566,310 897,843 534,118 91,341 252,314 697,540 439,091 6,553 - - - 440,630 10/16/2005 2,267,546 1,343,488 796,262 134,349 398,131 954,110 701,236 445,645 262,144 43,008 145,817 256,570 11/18/2005 6,186,598 5,190,451 2,726,298 543,949 1,939,866 1,008,159 3,919,052 3,846,963 1,930,036 409,600 1,541,735 54,049 12/15/2005 8,860,467 7,916,749 4,089,446 792,986 3,080,192 937,206 2,673,869 2,726,298 1,363,148 249,037 1,140,326 (70,953)01/16/2006 12,215,910 11,272,192 5,898,240 1,061,683 4,377,805 937,206 3,355,443 3,355,443 1,808,794 268,697 1,297,613 -02/15/2006 15,414,067 14,470,349 7,916,749 1,323,827 5,347,738 937,206 3,198,157 3,198,157 2,018,509 262,144 969,933 -03/15/2006 18,140,365 17,196,646 9,594,470 1,553,203 6,134,170 938,392 2,726,298 2,726,297 1,677,721 229,376 786,432 1,186 04/17/2006 22,124,954 21,286,093 12,006,195 1,939,866 7,392,461 938,392 3,984,589 4,089,447 2,411,725 386,663 1,258,291 -05/15/2006 25,375,539 24,641,536 13,841,203 2,241,331 8,545,894 938,392 3,250,585 3,355,443 1,835,008 301,465 1,153,433 -06/15/2006 28,940,698 28,101,837 15,833,498 2,582,118 9,646,899 938,392 3,565,159 3,460,301 1,992,295 340,787 1,101,005 -07/18/2006 31,037,850 29,989,274 17,406,362 3,001,549 9,646,899 938,392 2,097,152 1,887,437 1,572,864 419,431 - -08/15/2006 33,554,432 32,086,426 19,293,798 3,486,515 9,646,899 939,098 2,516,582 2,097,152 1,887,436 484,966 - 706 09/15/2006 35,861,299 34,393,293 21,390,950 3,722,445 9,646,899 939,098 2,306,867 2,306,867 2,097,152 235,930 - -10/16/2006 37,329,306 35,861,299 22,754,099 3,722,445 9,646,899 939,098 1,468,007 1,468,006 1,363,149 - - -11/17/2006 39,636,173 37,948,736 23,278,387 3,722,445 11,481,907 939,098 2,306,867 2,087,437 524,288 - 1,835,008 -12/15/2006 39,636,173 37,948,736 23,278,387 3,722,445 11,481,907 939,098 - - - - - -

Cumulative Injection Monthly Injection

Period End Date

Notes: The sanitary sewer discharge was redetermined on 12/15/05 based on the sewer meter. Previous values were from the recirculation meter. The difference, 71,000 gallons was pumped from the EQ tank, through the recirculation meter, through the air stripper and back into the EQ tank during the final startup period.

DFW\P\345406\T10\CSR_13\Table6-VolTreated PAGE 6 OF 8 December 2006

Table 7Summary Analytical Results From Influent and Effluent Water SamplingFruit Avenue Plume Superfund Site Albuquerque, New Mexico

Date

cis-1,2-Dichloro-

ethene Q

trans-1,2-Dichloro-

ethene QTrichloro-

ethene QJanuary 2005Q105ASTPINFLUENT1a N Influent 1/5/05 5.7 2.5 13Q105ASTPEFFLUENT1b N Effluent 1/5/05 1.0 U 1.0 U 1.0 UQ105ASTPINFLUENT2a N Influent 1/5/05 5.3 2.4 12Q105ASTPEFFLUENT2b N Effluent 1/5/05 1.0 U 1.0 U 1.0 UQ105ASTPINFLUENT3a N Influent 1/5/05 4.9 2.3 13Q105ASTPEFFLUENT3b N Effluent 1/5/05 1.0 U 1.0 U 1.0 UQ105ASTPINFLUENT4a N Influent 1/5/05 5.4 2.4 12Q105ASTPEFFLUENT4b N Effluent 1/5/05 1.0 U 1.0 U 1.0 UQ105ASTPEFFLUENT5b N Effluent 1/5/05 1.0 U 1.0 U 1.0 UFebruary 2005

N Influent 2/22/05 5.6 2.4 14N Effluent 2/22/05 1.0 U 1.0 U 1.0 U

March 2005N Influent 3/17/05 6 2.4 15N Effluent 3/17/05 1.0 U 1.0 U 1.0 U

October 2005FAP Infl 101905a N Influent 10/19/05 5.7 2.1 12FAP Treated 101905c N Effluent 10/19/05 0.7 J 1.0 U 1.0 UFAP Infl 102105a N Influent 10/21/05 5.3 2.2 12FAP Treated 102105c N Effluent 10/21/05 1.0 U 1.0 U 1.0 UFAP Infl 102505a N Influent 10/25/05 6.6 2.7 14FAP DUP 102505a QA/QC Influent 10/25/05 6.4 2.7 14FAP Treated 102505c N Effluent 10/25/05 0.8 J 1.0 U 1.0 UNovember 2005FAP SP-1 051130a N Influent 11/30/05 5 1.4 11FAP SP-5 051130c N Effluent 11/30/05 1.0 U 1.0 U 1.0 UJanuary 2006FAP SP-1 060109a N Influent 1/9/06 6.0 2.5 13FAP SP-2 060109d N Pretreated 1/9/06 6.1 2.4 13February 2006FAP SP-1 060127a N Influent 1/27/06 4.6 2.3 12FAP SP-5 060127c N Effluent 1/27/06 1.0 U 1.0 U 1.0 UMarch 2006FAP SP-1 060308a N Influent 3/8/06 4.3 1.5 13FAP SP-5 060308c N Effluent 3/8/06 1.0 U 1.0 U 1.0 UApril 2006FAP SP-1 060329a N Influent 3/29/06 5.0 1.0 12FAP SP-5 060329c N Effluent 3/29/06 1.0 U 1.0 U 1.0 UMay 2006Samples not collected for the May 2006 report

Sample Type& Location

DISCHARGE Cb

Sample ID

ASTP INFLUENTa

ASTP EFFLUENTb

ASTP INFLUENT Ca

DFW\P\345406\T10\CSR_13\Table7-WaterVOCs PAGE 7 OF 8 December 2006

Table 7Summary Analytical Results From Influent and Effluent Water SamplingFruit Avenue Plume Superfund Site Albuquerque, New Mexico

Date

cis-1,2-Dichloro-

ethene Q

trans-1,2-Dichloro-

ethene QTrichloro-

ethene QSample Type& LocationSample ID

June 2006FAP SP-1 060524 N Influent 5/24/06 4.7 1.9 12.8FAP SP-5 060524 N Effluent 5/24/06 0.5 U 0.5 U 0.5 UJuly 2006Samples not collected in time for the July 2006 reportAugust 2006FAP SP-1 0600719 N Influent 7/19/06 5.6 2.1 13.4FAP SP-5 0600719 N Effluent 7/19/06 0.5 U 0.5 U 0.5 USeptember 2006FAP SP-1 0600816 N Influent 8/16/06 5.6 1.9 13.6FAP SP-5 0600816 N Effluent 8/16/06 0.5 U 0.5 U 0.5 UOctober 2006FAP SP-1 061016 N Influent 10/16/06 4.6 1.7 11.6FAP SP-5 061016 N Effluent 10/16/06 0.5 U 0.5 U 0.5 UDecember 2006Samples not collected for the December 2006 report,due to system shut down.

Notes: Data Qualifier (Q): a Sample taken from sample port at ASTP influent line (SP1) U - the analyte was not detected b Sample taken from sample port after Air Stripper (SP3) B - the analyte was detected in an c Sample taken from sample port after treated water bag filter (SP5) associated blank d Sample taken from sample port after influent bag filter (SP2) Shaded cells indicate detected analytes J - the analyte was positively identified, N - normal sample but the quantitation is an estimation µg/L - micrograms per liter

Only analytical results for COC's are included in this table. Complete results are available in Attachment C - Analytical Laboratory Results.

DFW\P\345406\T10\CSR_13\Table7-WaterVOCs PAGE 7 OF 8 December 2006

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)01/04/2005 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.00002/01/2005 0.008 0.003 0.001 0.012 0.008 0.003 0.001 0.01203/01/2005 0.037 0.014 0.005 0.056 0.045 0.017 0.006 0.06804/01/2005 0.014 0.005 0.002 0.021 0.059 0.022 0.008 0.08905/01/2005 0.000 0.000 0.000 0.000 0.059 0.022 0.008 0.08906/01/2005 0.000 0.000 0.000 0.000 0.059 0.022 0.008 0.08907/01/2005 0.000 0.000 0.000 0.000 0.060 0.022 0.008 0.08908/01/2005 0.000 0.000 0.000 0.000 0.060 0.022 0.008 0.08909/15/2005 0.022 0.009 0.003 0.034 0.082 0.031 0.011 0.1210/16/2005 0.033 0.014 0.005 0.052 0.12 0.045 0.016 0.1811/18/2005 0.19 0.077 0.028 0.29 0.30 0.12 0.045 0.4712/15/2005 0.11 0.046 0.0091 0.16 0.41 0.17 0.054 0.6301/16/2006 0.16 0.070 0.025 0.25 0.57 0.24 0.079 0.8802/15/2006 0.12 0.042 0.019 0.18 0.69 0.28 0.098 1.0603/15/2006 0.13 0.039 0.010 0.18 0.81 0.32 0.109 1.2404/17/2006 0.17 0.068 0.008 0.25 0.99 0.39 0.116 1.4905/15/2006 0.14 0.055 0.006 0.20 1.13 0.44 0.122 1.6906/15/2006 0.17 0.060 0.022 0.25 1.30 0.50 0.144 1.9407/18/2006 0.10 0.035 0.013 0.15 1.40 0.54 0.157 2.0908/15/2006 0.13 0.051 0.018 0.19 1.52 0.59 0.175 2.2909/15/2006 0.12 0.047 0.014 0.18 1.64 0.64 0.189 2.4610/16/2006 0.06 0.024 0.008 0.10 1.70 0.66 0.197 2.5611/17/2006 0.10 0.038 0.013 0.15 1.80 0.70 0.210 2.7112/15/2006 0.00 0.000 0.000 0.00 1.80 0.70 0.210 2.71

Notes:The May 2005 through August 2005 data is the same as the April 2005 data because the ASTP was shut down from 3/24/05 through 9/8/05The May, July, and December 2006 quantities are estimated from the previous months process samples.

Table 8Summary of COC Mass RemovedFruit Avenue Plume Superfund Site

DFW\P\345406\T10\CSR_13\Table8-MassRemoved PAGE 9 OF 8 December 2006

FRUIT AVENUE PLUME SUPERFUND SITE CLEANUP STATUS REPORT 13 –NOVEMBER/DECEMBER 2006

VERSION 1.0



Figures


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R o m a A v e

D r M a r t i n L u t h e r K i n g J r A v e

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1st S

t

John

St

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nd

Bro

adw

ay B

lvd

Lomas Blvd

Fruit AvenuePlume Ground Water

Treatment System

BNSF Rail

D2E-P1

D2E/I3

I2/D1E-I1Air Stripper

Treatment Plant

Albuquerque RegionalMedical Center

Fruit Avenue Plume Site Boundary

Approximate Plume Boundary

Fruit Avenue Plume Superfund SiteAlbuquerque, NM

Figure 1

Source:

FILENAME: \\texan\is_proj\ J:\FruitAve\April2005\mxd\Figure1_SiteBoundary.mxd

LegendLTM Monitor Well Site Map

August 2005

0 250 500 750 1,000Feet

Existing and Potential Receptor WellsRailroadPipeline


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50Cumulative Extraction Well Flow Cumulative Treated Water Injected

Figure 3. Monthly and Cumulative Volume of Water Extracted and Injected

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5Monthly Extraction Well Flow Monthly Treated Water Injected


VERSION 1.0



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2.00

2.25

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2.75

3.00Cumulative TCE Removed Cumulative cDCE Removed Cumulative tDCE Removed Cumulative Total COCs Removed

Figure 4. Monthly and CumulativeContaminant Mass Removal

Jan-

05

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5

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5

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VERSION 1.0



Attachments


VERSION 1.0



Attachment A

Field Notes


VERSION 1.0



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CH2MHILL- FAP ASTP Inspection Data Log Form


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Inspection CataLog Fomuls


VERSION 1.0



Attachment C

COC Recovery Calculations


VERSION 1.0



Reporting Period Date

Extraction Well Totalizer

(gal)Begin October 16, 2006 37,329,306End December 15, 2006 39,636,173

Sample Location Sample ID Sample Date TCE cDCE tDCE UnitsInfluent water FAP SP-1 061016 10/16/2006 11.6 4.6 1.7 µg/LEffluent water FAP SP-5 061016 10/16/2006 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 = 11.6 µg/L = Average Concentration in SP-1 (influent) Water Sample 4.6 1.7CE = 0.3 µg/L = Average Concentration in SP-5 (Effluent) Water Sample 0.3 0.3ΔC = 11.4 µg/L = Concentration Removed 4.4 1.5V2 = 39,636,173 Gallons = Final Extraction Well Totalizer ReadingV1 = 37,329,306 Gallons = Initial Extraction Well Totalizer ReadingΔV = 2.31E+06 Gallons = Volume of Ground Water TreatedΔV = 8.73E+06 Liters = Volume of Ground Water Treated this Period 8.73E+06 8.73E+06

M (mass) = ΔC * ΔV * ( 10-9 kg/µg)= 11.4 µg/L * 8.73x10^6 Liters * 10-9 kg/ug

M (mass) = 0.10 Kilograms = Mass of Contaminant Removed from Ground Water this Period 0.038 0.013

Effective COC Recovery Calculation (Based on Water Concentration)Trichloroethene

Fundamental Values Data Table

Attachment CCOC Recovery Calculations

Fruit Avenue Plume Superfund Site - Air Stripper Treatment Plant, Albuquerque, New Mexico(October 16 to December 15, 2006)

DFW\P\345406\T10\CSR_13_Ver1.0\Attachment_C_ContamCalcs PAGE 1 OF 1 December 2006


VERSION 1.0



Monthly Cleanup Status Report – No. 13 Period of October ... · CLEANUP STATUS REPORT 13 –...

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