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Environmental Impact of Atmospheric Fugitive Emissions from Amine Based Post Combustion CO 2 Capture Moetaz I. Attalla, Merched Azzi, Phil Jackson, Dennys Angove Centre for Energy Technology, CSIRO, Newcastle, NSW, Australia and Centre for Energy Technology, CSIRO, Lucas Heights, NSW, Australia. contact: Moetaz Attalla phone: (+61) 2 4960 6083 email: [email protected] web: www.det.csiro.au Introduction Global reductions in greenhouse gas emissions are now recognised as a priority for combating climate change. However, since coal and gas fired electricity generation are likely to remain the largest sources of CO 2 emissions for the foreseeable future, CO 2 capture and storage is crucial technology if emission reductions are to be achieved. Major projects are currently being undertaken globally to adapt and improve carbon dioxide gas separation technologies for CO 2 post combustion capture (PCC) applications. The most mature technology for PCC is amine solvent-based chemical absorption/release of CO 2 . This technology is currently being applied at pilot scale and is likely to be the first technology successfully demonstrated and thereby reach commercial scale application. If solvent based PCC technology is deployed at a commercial scale, potentially millions of tonnes of solvent will be used per annum. Hence, fugitive emissions of solvents and solvent degradation products (through oxidative and thermal degradation) will likely occur. Some potential environmental concerns associated with these emissions include: Entrainment of the amine/ammonia with the treated flue gas and their associated atmospheric chemical reaction pathways (reactions with NO x , CO, O 2 ) Formation of ammonia and other amine degradation products such as formic acid, ethylamine, acetone etc., can be entrained with the flue gas to the atmosphere. In particular, NH 3 can enhance the formation of particulate matter in the atmosphere Nitrosamines formation as a result of reaction between an amine and nitrogen oxide The mounting evidence of the presence of amines in the particulate phase It is also known that amines in the atmosphere can be oxidised by OH•, O 3 and possibly by NO 3 • chemical reactions. In additions amines can react with nitrous acid (HONO) to produce nitrosamines which in turns can undergo photolysis to reproduce amine and NO. To ensure the viability of this technology, it is crucial at this early stage of development that a thorough understanding of the potential environmental impacts of fugitive emissions on terrestrial, aquatic and atmospheric environments be investigated. However, at present, there is little understanding of the environmental impact of PCC technology. The aim of the present work is to use controlled laboratory/ pilot scale experiments to determine the major chemical components emitted under different operation conditions. As well, the atmospheric photo-oxidation products of amines were studied in a smog chamber under ambient conditions. In this paper we present data where we have estimated the chemical compositions of potential fugitive emissions in the flue gases from the CO 2 capture system. Using the CSIRO smog chamber, the potential environmental impact of selected relevant compounds has been assessed in terms of their reactivities to produce secondary products. These secondary products were characterised to determine their potential health risk factors. As a result of this study, a chemical reaction scheme will be generated. The new mechanism will be incorporated into air quality model that can be used to assess the potential impact of using amine solutions for CO 2 capture. The results will be used to determine the trade-off between CO 2 capture and local and regional air quality. Acknowledgements This CSIRO Coal Portfolio research project has been funded by the Australian Government through the Asia Pacific Partnership on Clean Development and Climate initiative (APP). Field program Laboratory program CSIRO PCC pilot plant deployed to power station Loy Yang MEA Lake Munmorah NH 3 Tarong ?? ENVIRONMENTAL EMISSIONS ENVIRONMENTAL EMISSIONS Solvent system On-site sampling of: (i) pilot liquor (ii) lean CO 2 gas stream 200 250 300 350 400 450 500 EASTING (km) 6150 6200 6250 6300 6350 6400 NORTHING (km) SYDNEY MUSWELLBROOK NEWCASTLE PICTON WOLLONGONG PENRITH LITHGOW 40 50 60 70 80 90 100 110 120 HOUR 15 10 20 30 40 50 60 70 80 90 100 NOx O3 Modelling Plume Dispersion Lab-scale amine degradation apparatus 10 eV collision energy, pressure = 2.23e-3 m/z 10 20 30 40 50 60 70 80 90 100 % 0 100 Daughters of 89ES- Top: IR spectral surface between 2000-900 cm -1 for the reaction between aqueous 30.00 % wt MEA and a gas stream of 1.702 L/min containing 13.04 % CO 2 ; Bottom: CID of mass-selected oxalate anion at 10 eV collision energy. The peak at m/z 35 (H 3 O 2 - ) arises from a contaminant ion of mass m/z 89, most likely (H 2 O) 4 OH - . Oxalate has been identified as one of the major MEA decomposition products. 1 The CID result suggests a major thermal decomposition pathway leads to bicarbonate, the other major pathway to formate. Thus, oxalate slippage from a CO 2 capture plant operating with MEA could locally alter the biosphere pH; Left: HPLC-DAD and HPLC-MS + traces for a controlled MEA oxidation experiment conducted in the lab- scale amine degradation apparatus, top far left. Time 2.00 6.0 0 10.00 14.00 18.00 22.00 AU 0.0 1.0 2.0 2: Diode Array 3.40 5.27 8.84 % 0 100 1: Scan ES+ 3.40 5.33 9.02 2.00 6.00 10.00 14.00 18.00 22.00 Time The CSIRO photochemical smog chamber 0 100 200 300 0.01 0.1 1 10 100 ULP + MEA ULP SOA Mass conc. (μg/m 3 ) Time (min.) SOA mass conc. profiles for ULP (red) and ULP+ MEA (black) experiments 0 100 200 300 0 50 100 150 200 Concentration (ppb) Time (min.) Ozone NO NOy-NO NOy Ozone and NOx profiles for ULP (grey) and ULP+MEA (colours) experiments Merched Azzi (+61) 2 9710 6870 [email protected] www.det.csiro.au ATR-FTIR HPLC-MS/MS Realistic lab based data and analytical procedures: Oxidation and thermal degradation experiments carried out under controlled laboratory conditions Low limit-of-detection analytical procedures Pilot plant samples from exhaust and liquor: For long term operational data Smog chamber simulations will be carried out to: Identify the major pollutants produced by the photo-decomposition of the flue gas compounds of the absorber under selected ambient conditions Identify the major chemical reactions pathways responsible of the MEA oxidation Develop the appropriate chemical mechanism required to simulate the oxidation of MEA Airshed modelling to determine the potential environmental impact of using amine solution for CO 2 capture: Embedded the modified chemical mechanism into the airshed model Simulate different atmospheric scenarios to assess the potential impact of the new CO 2 capture process Determine the trade off between CO 2 capture and local and regional air quality Solvent development work to mitigate environmental impact. Current and Future Work HPLC-MS References 1. Goff, G.S.; Rochelle, G.T. Ind. Eng. Chem. Res. 2004, 43, 6400.

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Page 1: Environmental Impact of Atmospheric Fugitive … › docs › General_Docs › 12 cap › CSIRO Poster...Environmental Impact of Atmospheric Fugitive Emissions from Amine Based Post

Environmental Impact of Atmospheric Fugitive Emissions from Amine Based Post Combustion CO2 Capture

Moetaz I. Attalla, †Merched Azzi, Phil Jackson, †Dennys AngoveCentre for Energy Technology, CSIRO, Newcastle, NSW, Australia and †Centre for Energy Technology, CSIRO, Lucas Heights, NSW, Australia.

contact: Moetaz Attallaphone: (+61) 2 4960 6083email: [email protected]: www.det.csiro.au

Introduction Global reductions in greenhouse gas emissions are now recognised as a priority for combating climate change. However, since coal and gas fired electricity

generation are likely to remain the largest sources of CO2 emissions for the foreseeable future, CO2 capture and storage is crucial technology if emission reductions are to be achieved.

Major projects are currently being undertaken globally to adapt and improve carbon dioxide gas separation technologies for CO2 post combustion capture (PCC) applications. The most mature technology for PCC is amine solvent-based chemical absorption/release of CO2. This technology is currently being applied at pilot scale and is likely to be the first technology successfully demonstrated and thereby reach commercial scale application.

If solvent based PCC technology is deployed at a commercial scale, potentially millions of tonnes of solvent will be used per annum. Hence, fugitive emissions of solvents and solvent degradation products (through oxidative and thermal degradation) will likely occur. Some potential environmental concerns associated with these emissions include:• Entrainment of the amine/ammonia with the treated flue gas and their associated atmospheric chemical reaction pathways (reactions with NOx, CO, O2)• Formation of ammonia and other amine degradation products such as formic acid, ethylamine, acetone etc., can be entrained with the flue gas to the atmosphere. In

particular, NH3 can enhance the formation of particulate matter in the atmosphere• Nitrosamines formation as a result of reaction between an amine and nitrogen oxide • The mounting evidence of the presence of amines in the particulate phase

It is also known that amines in the atmosphere can be oxidised by OH•, O3 and possibly by NO3• chemical reactions. In additions amines can react with nitrous acid (HONO) to produce nitrosamines which in turns can undergo photolysis to reproduce amine and NO.

To ensure the viability of this technology, it is crucial at this early stage of development that a thorough understanding of the potential environmental impacts of fugitive emissions on terrestrial, aquatic and atmospheric environments be investigated. However, at present, there is little understanding of the environmental impact of PCC technology.

The aim of the present work is to use controlled laboratory/ pilot scale experiments to determine the major chemical components emitted under different operation conditions. As well, the atmospheric photo-oxidation products of amines were studied in a smog chamber under ambient conditions.

In this paper we present data where we have estimated the chemical compositions of potential fugitive emissions in the flue gases from the CO2 capture system. Using the CSIRO smog chamber, the potential environmental impact of selected relevant compounds has been assessed in terms of their reactivities to produce secondary products. These secondary products were characterised to determine their potential health risk factors.

As a result of this study, a chemical reaction scheme will be generated. The new mechanism will be incorporated into air quality model that can be used to assess the potential impact of using amine solutions for CO2 capture. The results will be used to determine the trade-off between CO2 capture and local and regional air quality.

AcknowledgementsThis CSIRO Coal Portfolio research project has been funded by the Australian Government through the Asia Pacific Partnership on Clean Development and Climate initiative (APP).

Field program

Laboratory program

CSIRO PCC pilot plant deployed to power station

Loy Yang MEALake Munmorah NH3Tarong ??

ENVIRONMENTALEMISSIONS

ENVIRONMENTALEMISSIONS

Solvent system

On-site sampling of:(i) pilot liquor(ii) lean CO2 gas stream

200 250 300 350 400 450 500EASTING (km)

6150

6200

6250

6300

6350

6400

NORT

HING

(km)

SYDNEY

MUSWELLBROOK

NEWCASTLE

PICTON

WOLLONGONG

PENRITH

LITHGOW

40

50

60

70

80

90

100

110

120

HOUR 15

102030405060708090100

NOx

O3

Modelling PlumeDispersion

Lab-scale amine degradation apparatus

10 eV collision energy, pressure = 2.23e-3

m/z10 20 30 40 50 60 70 80 90 100

%

0

100

Daughters of 89ES-

Top: IR spectral surface between 2000-900 cm-1 for the reaction between aqueous 30.00 % wt MEA and a gas stream of 1.702 L/mincontaining 13.04 % CO2; Bottom: CID of mass-selected oxalate anionat 10 eV collision energy. The peak at m/z 35 (H3O2

−) arises from acontaminant ion of mass m/z 89, most likely (H2O)4OH−. Oxalate hasbeen identified as one of the major MEA decomposition products.1The CID result suggests a major thermal decomposition pathway leadsto bicarbonate, the other major pathway to formate. Thus,oxalate slippage from a CO2 capture plant operating with MEAcould locally alter the biosphere pH; Left: HPLC-DAD and HPLC-MS+

traces for a controlled MEA oxidation experiment conducted in the lab-scale amine degradation apparatus, top far left.

Time2.00 6.00

10.00 14.00 18.00 22.00

AU

0.0

1.0

2.0

2: Diode Array 3.40

5.27

8.84

%

0

100 1: Scan ES+ 3.40

5.339.02

2.00 6.00 10.00 14.00 18.00 22.00 Time

The CSIRO photochemical smog chamber

0 100 200 3000.01

0.1

1

10

100

ULP + MEAULP

SO

A M

ass

conc

. (µg

/m3 )

Time (min.)

SOA mass conc. profiles for ULP (red) and ULP+ MEA (black) experiments

0 100 200 3000

50

100

150

200

Con

cent

ratio

n (p

pb)

Time (min.)

Ozone NO NOy-NO NOy

Ozone and NOx profiles for ULP (grey) andULP+MEA (colours) experiments

Merched Azzi(+61) 2 9710 [email protected]

ATR-FTIR

HPLC-MS/MS

Realistic lab based data and analytical procedures:• Oxidation and thermal degradation experiments carried out under controlled laboratory conditions • Low limit-of-detection analytical procedures

Pilot plant samples from exhaust and liquor: • For long term operational data

Smog chamber simulations will be carried out to:• Identify the major pollutants produced by the photo-decomposition of the flue gas compounds of the absorber under

selected ambient conditions• Identify the major chemical reactions pathways responsible of the MEA oxidation• Develop the appropriate chemical mechanism required to simulate the oxidation of MEA

Airshed modelling to determine the potential environmental impact of using amine solution for CO2 capture:• Embedded the modified chemical mechanism into the airshed model• Simulate different atmospheric scenarios to assess the potential impact of the new CO2 capture process• Determine the trade off between CO2 capture and local and regional air quality

Solvent development work to mitigate environmental impact.

Current and Future Work

HPLC-MS

References1. Goff, G.S.; Rochelle, G.T. Ind. Eng. Chem. Res. 2004, 43, 6400.