현대오일뱅크

Capacity 24,000 N㎥/hr
Organic Content2~3 g/㎥
Application Tank Vent Gas, Process Vent, WWT Vent Gas
HeaterGas Burner
TypeOne Cantype RTO
Construction2013. 05.
Main ComponentBTX compound

(주)지흥 파주공장

Capacity110,000 Nm3/hr
Organic Content1,000 ppm
Application Process Gas, Toluene, I.P.A, M.E.K
HeaterLNG Burner
TypeOne Can
Construction2008. 12.
Main componentTHC

인스콘테크(주) 안성공장

Capacity110,000 Nm3/hr
Organic Content1,000 ppm
Application Process Gas, Toluene, I.P.A, M.E.K
HeaterLNG Burner
TypeOne Can
Construction2008. 09.
Main componentTHC

삼성전기(주)

Capacity24,000 Nm3/hr
Organic Content2 ∼ 3 g/m3
Application Process Vent Gas, Toluene, I.PA, M.E.K
HeaterGas Burner
Type2Bed RTO
Construction2006. 07.
Main componentToluene, I.PA, M.E.K

삼성전기(주)

Capacity15,000 m3/hr
Organic Content2~3 g/m3
Application Process Vent Gas, Toluene, I.PA, M.E.K
HeaterGas Burner
Type3Bed RTO + Heat Exchanger
Construction2005. 04.
Main componentToluene, I.PA, M.E.K

삼성전기(주)

Capacity18,000 m3/hr
Organic Content2 ∼ 3 g/m3
Application Process Vent Gas, Toluene, I.PA, M.E.K
HeaterGas Burner
Type3Bed RTO + Heat Exchanger
Construction2005. 04.
Main componentToluene, I.PA, M.E.K

삼성전기(주)

Capacity32,000 m3/hr
Organic Content2~3 g/m3
Application Process Vent Gas, Toluene, I.PA, M.E.K
HeaterGas Burner
Type3Bed RTO + Heat Exchanger
Construction2005. 03.
Main componentToluene, I.PA, M.E.K

삼성전기(주)

Capacity40,000 m3/hr
Organic Content2 ∼ 3 g/m3
Application Process Vent Gas, Toluene, I.PA, M.E.K
HeaterGas Burner
Type3Bed RTO + Heat Exchanger
Construction2005. 03.
Main componentToluene, I.PA, M.E.K

삼성SDI(주)

Capacity9,000 m3/hr
Organic Content2~3 g/m3
Application Process Vent Gas
HeaterGas Burner
TypeOne Cantype RTO + Heat Exchanger
Construction2004. 11.
Main componentToluene, M.E.K

국토 정밀 화학

Capacity40,000 m3/hr
Organic Content6 g/m3
Application Process Vent Gas
HeaterGas Burner
Type3Bed RTO + Heat Exchanger
Construction2003. 08.
Main componentToluene

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