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KISS
A simplified procedure is proposed for the desulfurization by means of the catalytic reaction of alkali-ferrite. The vapor of gas oil shall be passed over the catalyst containing alkali-ferrite supported on an inert carrier such as aluminium oxide. Th...
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RISS 인기검색어
Alkali Ferrite 촉매에 의한 경유의 탈황에 관한 연구 = Catalytic Desulfurization from Hydrocarbons in the Vapor Phase by Alkali - Ferrite
한글로보기https://www.riss.kr/link?id=A3087668
- 저자
- 발행기관
- 학술지명
- 권호사항
-
발행연도
1972
-
작성언어
-
-
KDC
500
-
등재정보
SCOPUS,KCI등재,ESCI
-
자료형태
학술저널
- 발행기관 URL
-
수록면
33-37(5쪽)
- 제공처
- 소장기관
-
0
상세조회 -
0
다운로드
부가정보
다국어 초록 (Multilingual Abstract)
A simplified procedure is proposed for the desulfurization by means of the catalytic reaction of alkali-ferrite. The vapor of gas oil shall be passed over the catalyst containing alkali-ferrite supported on an inert carrier such as aluminium oxide. The alkali in the ferrite is potassium oxide or sodium oxide. The reaction temperature of catalyst shall be modified between 300℃ and 450℃, and the pressure atmospheric, and the feed rate of gas oil is 50㎖/hr. The sulfur content of the feed gas oil is 1.09 %. As the result, the efficiency of desulfurization has been about 60%, and the best conditions for catalytic desulfurization were as follow: 1) Alkali in the catalyst … potassium oxide. 2) Ratio of alkali oxide to ferric oxide … 1/1 (molar). 3) Ratio of alkali-ferrite to alumina … 1/1(weight). 4) Temperature of catalyst in the reactor … 400-450℃ at atmospheric pressure.
A simplified procedure is proposed for the desulfurization by means of the catalytic reaction of alkali-ferrite. The vapor of gas oil shall be passed over the catalyst containing alkali-ferrite supported on an inert carrier such as aluminium oxide. The alkali in the ferrite is potassium oxide or sodium oxide. The reaction temperature of catalyst shall be modified between 300℃ and 450℃, and the pressure atmospheric, and the feed rate of gas oil is 50㎖/hr. The sulfur content of the feed gas oil is 1.09 %. As the result, the efficiency of desulfurization has been about 60%, and the best conditions for catalytic desulfurization were as follow: 1) Alkali in the catalyst … potassium oxide. 2) Ratio of alkali oxide to ferric oxide … 1/1 (molar). 3) Ratio of alkali-ferrite to alumina … 1/1(weight). 4) Temperature of catalyst in the reactor … 400-450℃ at atmospheric pressure.
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