corona-discharge treatment of gaseous benzene, toluene and

1
2.0 1.5 1.0 0.5 0.0 800 750 700 650 600 wavenumber [cm -1 ] 2.0 1.5 1.0 0.5 0.0 absorbance [a.u.] 2.0 1.5 1.0 0.5 0.0 2000 1500 1000 500 0 number of carbon atoms [ppm] 60 50 40 30 20 10 0 input energy [kJ] CO 2 CO HCOOH C 6 H 4 (CH 3 ) 2 AFAH FAH minor products 2000 1500 1000 500 0 number of carbon atoms [ppm] 60 50 40 30 20 10 0 input energy [kJ] AFAH FAH minor products CO 2 CO HCOOH C 6 H 5 CH 3 1500 1000 500 0 number of carbon atoms [ppm] 60 50 40 30 20 10 0 input energy [kJ] FAH minor products CO 2 CO HCOOH C 6 H 6 400 300 200 100 0 concentration [ppm] 50 40 30 20 10 0 input energy [kJ] HCOOH 500 400 300 200 100 0 concentration [ppm] 50 40 30 20 10 0 input energy [kJ] CO 1000 800 600 400 200 0 concentration [ppm] 50 40 30 20 10 0 input energy [kJ] CO 2 400 300 200 100 0 concentration [ppm] 50 40 30 20 10 0 input energy [kJ] C 6 H 6 C 6 H 5 CH 3 C 6 H 4 (CH 3 ) 2 300 250 200 150 100 50 0 amount of emissions [kt/year] Corona-discharge treatment of gaseous benzene, toluene and xylene at atmospheric pressure Kohji Nagao 1 , Kohki Satoh 1,2 and Hidenori Itoh 1 1 Graduate school of Engineering, Muroran Institute of Technology, Muroran 050-8585, Japan 2 Center of Environmental Science and Disaster Mitigation for Advanced Research, Muroran Institute of Technology, Muroran 050-8585, Japan Email : [email protected] 2. Experimental apparatus and conditions Discharge chamber The cylindrical discharge chamber is made of stainless-steel, with 197 mm inner diameter and 300 mm height. Applied voltage A positive DC high voltage (20 ~ 28 kV) is applied to the multi-needle electrode, generating a streamer corona discharge. Electrodes A multi-needle electrode, which consists of thirteen stainless-steel needles (55 mm length and 4 mm diameter) and a plane electrode made of stainless steel (80 mm diameter), are placed in a cylindrical discharge chamber. The distance between the multi-needle electrode and the plane electrode is fixed at 35 mm. Gas conditions Nitrogen-oxygen mixture is used as a background gas, and the mixture ratio is N 2 :O 2 = 80:20 %. Initial gas pressure in the chamber is 1013 hPa (atmospheric pressure), and initial concentrations of benzene, toluene and xylene are 300 ppm. Concentration measurement Concentrations of benzene, toluene, xylene and by-products are measured by a Fourier Transform Infrared Spectrophotometer (Shimadzu, FTIR- 8900) equipped with a gas cell (Infrared Analysis, 10PA), which has optical path length of 10 m. Measurement of voltage and current Applied voltage is measured by a high-voltage probe (Tektronix P6015A). Discharge current is calculated by voltage drop across a non-inductive resistance (1 kW), which is connected between the plane electrode and the earth. 1. Introduction Objective We investigate the decomposition characteristics of benzene, toluene and xylene in an atmospheric DC corona discharge. Concentration variations of benzene, toluene, xylene and by-products are measured by infrared spectroscopy, and then the decomposition processes of benzene, toluene and xylene is examined. Recently, various kinds of VOCs (volatile organic compounds) contained in exhaust gas from factories, automobiles, etc., cause major environmental issues. Toluene (C 6 H 5 CH 3 ) and xylene (C 6 H 4 (CH 3 ) 2 ) are emitted to the environment in the largest volume. toluene (41%) xylene (26%) benzene (4%) The emission volume of benzene (C 6 H 6 ) is less than those of toluene and xylene, but it has carcinogenicity and teratogenicity. PRTR (Pollutant Release and Transfer Register) data in 2007 [1] ethlbenzene methylene chloride poly oxyethylene = alkyl ether p-dichlorobenzene [1] Ministry of the Environment of japanThe compendium of PRTR data on 2007 (released in 2009). benzene (C 6 H 6 ) toluene (C 6 H 5 CH 3 ) xylene (C 6 H 4 (CH 3 ) 2 ) Approaches to decompose VOCs using discharge plasmas have attracted attention. Decomposition processes of benzene, toluene and xylene in nitrogen-oxygen mixture gas in an atmospheric DC corona discharge are investigated. CO 2 , CO, HCOOH, formic anhydride (FAH), C 2 H 2 , HCN, maleic anhydride and glyoxal are produced from benzene in the atmospheric DC corona discharge. Acetic formic anhydride (AFAH), peroxyacethyl nitrate, CH 4 , HCHO, CH 3 COOH and methyl glyoxal are produced from only toluene and xylene. Concentrations of benzene, toluene and xylene decrease monotonously with the increase of input energy. Benzene, toluene and xylene are chiefly converted to CO 2 via CO, HCOOH, FAH andAFAH by the atmospheric DC corona discharge. Some of carbon atoms containing in benzene, toluene and xylene are deposited on the electrodes and the wall of the discharge chamber. 3. Results and discussion 4. Conclusions (3) Mass balance for carbon atoms The total number of carbon atoms, which is presented as the top line of stacked graph, decreases monotonously with the increase of input energy, and then becomes constant. × number of carbon atoms in each of gaseous molecules concentration [ppm] The number of carbon atoms [ppmC] C 6 H 6 C 6 H 5 CH 3 C 6 H 4 (CH 3 ) 2 CO 2 is a gaseous end product, and the other products are intermediate products. (2) Concentration variations of benzene, toluene, xylene and major by-products Concentrations of benzene, toluene and xylene decrease with the increase of input energy. CO 2 , CO, HCOOH, FAH andAFAH are major by-products from benzene, toluene and xylene. (4) Decomposition processes of benzene, toluene and xylene Benzene, toluene and xylene are chiefly converted to CO 2 via CO, HCOOH, FAH and AFAH by the atmospheric DC corona discharge. The some of carbon atoms are deposited on the electrodes and the wall of the discharge chamber. (1) Infrared absorbance spectra CO 2 , CO, HCOOH, formic anhydride and acetic formic anhydride are produced from toluene. By-products from xylene are the same as those from toluene. 2.0 1.5 1.0 0.5 0.0 3500 3000 2500 2000 1500 1000 500 wavenumber [cm -1 ] 2.0 1.5 1.0 0.5 0.0 absorbance [a.u.] 2.0 1.5 1.0 0.5 0.0 without discharge with discharge (10 kJ) C 6 H 5 CH 3 after separation 2.0 1.5 1.0 0.5 0.0 800 750 700 650 600 wavenumber [cm -1 ] 2.0 1.5 1.0 0.5 0.0 absorbance [a.u.] 2.0 1.5 1.0 0.5 0.0 2.0 1.5 1.0 0.5 0.0 3500 3000 2500 2000 1500 1000 500 wavenumber [cm -1 ] 2.0 1.5 1.0 0.5 0.0 absorbance [a.u.] 2.0 1.5 1.0 0.5 0.0 without discharge with discharge (10 kJ) C 6 H 6 after separation CO 2 , CO, HCOOH and formic anhydride are produced from benzene. O 3 and N 2 O are produced from the background gas. C 6 H 6 CO 2 CO HCOOH N 2 O O 3 C 6 H 6 CO 2 C 6 H 6 formic anhydride (FAH) C 6 H 5 CH 3 C 6 H 5 CH 3 C 6 H 5 CH 3 CO 2 CO N 2 O O 3 CO 2 HCOOH 80 60 40 20 0 concentration [ppm] 50 40 30 20 10 0 input energy [kJ] FAH 50 40 30 20 10 0 concentration [ppm] 50 40 30 20 10 0 input energy [kJ] AFAH This leads that the some of carbon atoms containing in benzene, toluene and xylene are deposited on the electrodes and the wall of the discharge chamber. C 6 H 6 C 6 H 5 CH 3 C 6 H 4 (CH 3 ) 2 only C 6 H 5 CH 3 and C 6 H 4 (CH 3 ) 2 AFAH FAH HCOOH CO CO 2 fragments or by-products deposit FAH acetic formic anhydride (AFAH) CH 4 HCHO CH 3 COOH methyl glyoxal peroxyacetyl nitrate AFAH CO 2 CO HCOOH FAH maleic anhydride glyoxal C 6 H 6 C 2 H 2 HCN minor products By-products from benzene, toluene and xylene C 6 H 4 (CH 3 ) 2 C 6 H 5 CH 3

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Page 1: Corona-discharge treatment of gaseous benzene, toluene and

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Corona-discharge treatment of gaseous benzene, toluene and xylene

at atmospheric pressure

Kohji Nagao1, Kohki Satoh1,2 and Hidenori Itoh1

1 Graduate school of Engineering, Muroran Institute of Technology, Muroran 050-8585, Japan2 Center of Environmental Science and Disaster Mitigation for Advanced Research, Muroran Institute of Technology, Muroran 050-8585, Japan

Email : [email protected]

2. Experimental apparatus and conditions

Discharge chamber

• The cylindrical discharge chamber is made of

stainless-steel, with 197 mm inner diameter and

300 mm height.

Applied voltage

• A positive DC high voltage (20 ~ 28 kV) is applied

to the multi-needle electrode, generating a streamer

corona discharge.

Electrodes

• A multi-needle electrode, which consists of thirteen

stainless-steel needles (55 mm length and 4 mm

diameter) and a plane electrode made of stainless

steel (80 mm diameter), are placed in a cylindrical

discharge chamber.

• The distance between the multi-needle electrode

and the plane electrode is fixed at 35 mm.

Gas conditions

• Nitrogen-oxygen mixture is used as a background gas, and the mixture ratio is N2:O2 = 80:20 %.

• Initial gas pressure in the chamber is 1013 hPa (atmospheric pressure), and initial concentrations of benzene, toluene and xylene are 300 ppm.

Concentration measurement

• Concentrations of benzene, toluene, xylene and by-products are measured by a Fourier Transform Infrared Spectrophotometer (Shimadzu,

FTIR- 8900) equipped with a gas cell (Infrared Analysis, 10PA), which has optical path length of 10 m.

Measurement of voltage and current

• Applied voltage is measured by a high-voltage probe (Tektronix P6015A).

• Discharge current is calculated by voltage drop across a non-inductive resistance (1 kW), which is connected between the plane electrode and

the earth.

1. Introduction

Objective

We investigate the decomposition characteristics of benzene, toluene and xylene in an atmospheric DC

corona discharge. Concentration variations of benzene, toluene, xylene and by-products are measured by

infrared spectroscopy, and then the decomposition processes of benzene, toluene and xylene is examined.

Recently, various kinds of VOCs (volatile organic compounds) contained in exhaust gas

from factories, automobiles, etc., cause major environmental issues.

Toluene (C6H5CH3) and xylene (C6H4(CH3)2)

are emitted to the environment in the largest

volume.

toluene (41%)xylene (26%)

benzene (4%) The emission volume of benzene (C6H6) is

less than those of toluene and xylene, but it

has carcinogenicity and teratogenicity.

PRTR (Pollutant Release and Transfer Register) data in 2007[1]

ethlbenzene

methylene chloride

poly oxyethylene = alkyl ether

p-dichlorobenzene

[1] Ministry of the Environment of japan:The compendium of PRTR data on 2007 (released in 2009).

benzene (C6H6) toluene (C6H5CH3) xylene (C6H4(CH3)2)

Approaches to decompose VOCs

using discharge plasmas have

attracted attention.

Decomposition processes of benzene, toluene and xylene in nitrogen-oxygen mixture gas in an atmospheric DC corona discharge are investigated.

CO2, CO, HCOOH, formic anhydride (FAH), C2H2, HCN, maleic anhydride and glyoxal are produced from benzene in the atmospheric DC corona discharge.

Acetic formic anhydride (AFAH), peroxyacethyl nitrate, CH4, HCHO, CH3COOH and methyl glyoxal are produced from only toluene and xylene.

Concentrations of benzene, toluene and xylene decrease monotonously with the increase of input energy.

Benzene, toluene and xylene are chiefly converted to CO2 via CO, HCOOH, FAH and AFAH by the atmospheric DC corona discharge.

Some of carbon atoms containing in benzene, toluene and xylene are deposited on the electrodes and the wall of the discharge chamber.

3. Results and discussion

4. Conclusions

(3) Mass balance for carbon atoms

The total number of carbon atoms, which is presented as the top line of stacked graph, decreases

monotonously with the increase of input energy, and then becomes constant.

×number of carbon atoms in each of gaseous molecules concentration [ppm]

The number of carbon atoms [ppmC]

C6H6 C6H5CH3 C6H4(CH3)2

CO2 is a gaseous end product, and the other products are intermediate products.

(2) Concentration variations of benzene, toluene, xylene and major by-products

Concentrations of benzene, toluene and xylene decrease with the increase of input energy.

CO2, CO, HCOOH, FAH and AFAH are major by-products from benzene, toluene and xylene.

(4) Decomposition processes of benzene, toluene and xylene

Benzene, toluene and xylene are chiefly

converted to CO2 via CO, HCOOH, FAH and

AFAH by the atmospheric DC corona

discharge.

The some of carbon atoms are deposited on the

electrodes and the wall of the discharge

chamber.

(1) Infrared absorbance spectra

CO2, CO, HCOOH, formic anhydride and acetic formic anhydride are produced from toluene.

By-products from xylene are the same as those from toluene.

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without discharge

with discharge (10 kJ)

C6H5CH3

after separation

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without discharge

with discharge (10 kJ)

C6H6

after separation

CO2, CO, HCOOH and formic anhydride are produced from benzene.

O3 and N2O are produced from the background gas.

C6H6

CO2CO

HCOOHN2O O3

C6H6

CO2

C6H6

formic anhydride (FAH)

C6H5CH3

C6H5CH3

C6H5CH3

CO2CO

N2O O3 CO2HCOOH

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FAH50

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AFAH

This leads that the some of carbon atoms containing in benzene, toluene and xylene are deposited on

the electrodes and the wall of the discharge chamber.

C6H6

C6H5CH3

C6H4(CH3)2only C6H5CH3 and C6H4(CH3)2

AFAH

FAH

HCOOH

CO

CO2

fragments or by-products deposit

FAHacetic formic anhydride (AFAH)

CH4

HCHO

CH3COOH

methyl glyoxal

peroxyacetyl nitrate

AFAHCO2

CO

HCOOH

FAH

maleic anhydride

glyoxal

C6H6

C2H2

HCN

minor products

By-products from benzene, toluene and xylene

C6H4(CH3)2C6H5CH3