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PCK Schwedt refinery site Long term groundwater monitoring and natural attenuation Patrick Jacobs, Tauw Germany

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Page 1: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

PCK Schwedt refinery site

Long term groundwater monitoring and natural attenuation

Patrick Jacobs, Tauw Germany

Page 2: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

2

Project site, North-East Germany

Refinery site PCK Schwedt

Berlin

Germany

Page 3: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Location

Welse River Oder

Refinery site PCK Schwedt

Page 4: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Production areas

Verladung

AWBA

WZF

Tank farm

Former fertilizer production Hydrocarbon

production Tank farm

Page 5: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Site history

1974 1981

Page 6: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Substances handled

- Petrol,

- Diesel

- Kerosin (Jet A1)

- Fuel oil,

- MTBE + ETBE,

- BTEX, …

Page 7: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Ongoing water production andcontainment: total abstraction rate 3 · 106 m³ per year

Verladung

AWBA

WZF

LNAPL recovery (dynamic) Local GW

remediation

Local GW remediation

Groundwater abstraction

Page 8: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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LNAPL and BTEX in groundwater (2011)

Page 9: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

What is the problem to be solved?

•   Huge potential of hydrocarbons results in long-term release to the groundwater.

•   Options for source remediation strongly limited by lack of accessibility

•   Hydraulic containment results in large-scale draw down and vertical LNAPL dislocation

MNA or ENA are most promising options for a sustainable management

Page 10: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Approach: Site characterization and analysis of ongoing NA processes

Geo-hydraulic conditions

Redox environment (monitoring sensitive parameters; screening tool: BOS-NA)

Contaminant plume development with time (trend analysis using Mann-Kendall test)

Evidence for microbial degradation by specific metabolites

Efficiency of natural attenuation by analysis of flow lines

Mass balances of contaminants

Page 11: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

Investigation of NA potential: redox processes

Page 12: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Groundwater monitoring since 1970

•   Number of monitoring wells: ~ 420 •   Sampling campaigns: 2 per year

•   Parameters: -   Meteorological data, groundwater recharge

-   Groundwater abstraction rates

-   Water level data (~ 420 piezometers)

-   LNAPL thickness

-   Contaminant concentration (BTEX, MTBE, etc., ca. 100 – 200 wells)

-   Redox parameters (O2, NO3, SO4, S-, Fe, Mn, CH4)

-   Fe, Mn, CH4, CO2/HCO3, specific metabolites

•   Data management tool: GeODin

Page 13: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Favorable redox conditions vor NA? Screening scheme from the Dutch BOS-NA

Sulfate reduction / methane formation at / near source areas

Nitrate reduction downstream the former fertilizer production

Page 14: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

Evidence for anaerobic degradation from specific metabolites?

•  Benzyl succinic acid •  Benzoic acid (unspecific)

•  2,3-dimethyl benzoic acid

•  3,4-dimethyl benzoic acid

•  3,5-dimethyl benzoic acid

•  p-Tolylacetic acid (unspec.)

•  Methylbenzene (Toluene) •  Ethylbenzene

•  Dimethylbenzene

•  Trimethylbenzene

•  Methylethylbenzene

Educts Metabolites

Page 15: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

0,000

50,000

100,000

150,000

200,000

250,000

Sulfatre

dukti

on

Fe Red

uktio

n, Sulfa

tredu

ktion

Fe Red

uktio

n, Sulfa

tredu

ktion

Fe Red

uktio

n, Sulfa

tredu

ktion

Fe-Red

uktion

Fe-Red

uktion

Fe-Red

uktion

Fe-Red

uktion

Fe-Red

uktion

Fe-Red

uktion

Nitratre

dukti

on

Nitratre

dukti

on

Nitratre

dukti

on, o

xisch

Nitratre

dukti

on, o

xisch

oxisc

h

Summe Dimethyl-benzoesäurep-Tolyl-essigsäureBenzyl-BernsteinsäureBenzoesäure

Metabolite occurrence in different redox settings

sulfate red.

iron reduction

nitrate red.

aerobic

µg/L

Page 16: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Benzene degradation according to mass balance vs. upstream TEA

Stoffumsatz t Benzen pro Jahr

Sulfatreduzierend; 16,6

Methanogenese; 7,5

Aerob/ nitratreduzierend; 2,2

Eisenreduzierend; 0,85

Methane formation 7,5 t (28 %)

Aerobic / Nitrate 2,2 t (8 %)

Iron reduction 0,9 t (3 %)

Sulfate reduct. 16,6 t (61,1 %)

Page 17: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

Investigation of plume stability

Page 18: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

Statistical evaluation of NA effectiveness using Mann-Kendall (MK) test

•  Mainly stagnant conditions in the source zone

indicating a continuous contaminant supply.

•  Local concentration trends are mainly associated with

groundwater abstraction.

•  Analysis of the plume status in the sense of MNA is not

possible in the zone influenced by extraction wells.

Page 19: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Analyzing NA effectiveness along flow lines

Schadenseintrag

Methanogenese

Sulfatreduktion

Nitratreduktion

AWBA 1-4

Fe/Mn-Reduktion

GW

range analysed

Page 20: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Monitoring

Monitoring KORA (Test Site)

k [d-1] T(1/2) [d] k [d-1] T(1/2) [d]

Benzene 0,0016 430 d 0,003 – 0,042

0,03 17 - 230 d

23 d

Toluene 0,0073 95 d 0,066 – 0,439

0,09 2 – 11 d

7 d

Ethylbenzene 0,0010 690 d

Xylene 0,0013 530 d

Analyzing NA effectiveness along flow lines

Ø Ø

Ø Ø

Abbaubarkeit von Aromaten nach A. Geller

Page 21: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

NA based groundwater management concept

Page 22: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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IGM concept

•   Concept IGM = Integrated Grondwater Management •   Largescale contamination requires integral approach to

remediation •   (Re-)infiltration of (ground) water with high TEA concentrations

•   to compensate groundwater abstraction from containment and

process water production

•   to stabilise ground water levels and, by that, to avoid smearing of the

LNAPL layers

•   to enhance microbial degradation

Page 23: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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IGM concept

•  Pilot-scale infiltration of stormwater runoff and water drained from the adjacent agricultural land

•   NO3 > 10 mg/L •   SO4 ca. 200 mg/L

Page 24: PCK Schwedt refinery site - ABAS...Refinery site PCK Schwedt 4 Production areas Verladung AWBA WZF Tank farm Former fertilizer production Hydrocarbon production Tank farm 5 Site history

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Summary

•  Analysing the redox environment, the specific metabolites, and the field degradation rates in concert with balancing the TEA mass flow with the groundwater showed effective contaminant degradation at anaerobic conditions.

•  The contaminant plumes were shown to be largely stable or retrograding.

•  An integrated management concept including the amendment with TEAs is expected to increase the efficiency of the NA processes.