KR950000841A - 정제된 고온 가스 제조를 위한 부분 산화방법 - Google Patents

정제된 고온 가스 제조를 위한 부분 산화방법 Download PDF

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KR950000841A
KR950000841A KR1019940013701A KR19940013701A KR950000841A KR 950000841 A KR950000841 A KR 950000841A KR 1019940013701 A KR1019940013701 A KR 1019940013701A KR 19940013701 A KR19940013701 A KR 19940013701A KR 950000841 A KR950000841 A KR 950000841A
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gas
gas stream
alkali metal
sulfur
fuel
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프레드릭 레닌저 토마스
모리스 로빈 알렌
케니쓰 울펜바거 제임스
머레이 서지트 로버트
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알. 에프. 윌슨
텍사코 디벨롭프먼트 코포레이션
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Abstract

본 발명은 NH3를 포함하거나 포함하지 않고, 미립자 물질, 알칼리금속 화합물, 할로겐화수소, 시안화수소, 황을 함유하는 가스가 실질적으로 없는, 합성 가스, 환원 가스 또는 연료 가스용의 정제된 고온 가스기류를 제조하기 위한 부분 산화방법에 관한 것이다. 액체 탄화수소질 연료 또는 이들의 액체 에멀젼, 석유 코크스의 수성 슬러리, 및 이들의 혼합물로부터 선택된, 할로겐화물, 알칼리금속 화합물, 황, 질소 및 무기회분을 함유하는 펌프할수 있는 연료는 부분 산화에 의하여, H2, CO, CO2, H2O, CH4, NH3, HCN, HCl, HF, H2S, COS, N2, Ar, 미립자 물질, 증기상 알칼리금속 화합물, 용융 슬래그를 함유하는 고온의 원료 가스기류를 제조한다. 상기한 고온의 원료 가스기류는 냉각되고 세척된다. 임의로, 암모니아는 촉매적으로 N2와 H2로 불균등화되어 제거된다. 가공중의 가스기류는 냉각되어 가스기류중의 할로겐화물과 HCN은 HCl, HF, HCN을 제거하기 위한 보충 알칼리금속 화합물과 반응한다. 할로겐화 알칼리금속과 시안화 알칼리금속, 증기화된 알칼리금속 화합물과 잔류 초미립자 물질은 재냉각 및 여과에 의해 제거된다. 가공중의 가스기류내의 황을 함유하는 기체는 고온에서 혼합 금속 산화물 황 흡수제와 반응하여 적어도 540℃의 정제된 고온의 청정 가스기류에서 분리된 황화된 흡수제를 생성한다.

Description

정제된 고온 가스 제조를 위한 부분 산화방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명에 따른 방법의 한 구현예를 도시화한 것이다.

Claims (12)

  1. (1) 펌프할수 있는 탄화수소질 연료 원료공급원을 유리 산소를 함유하는 기체로 부분 산화반응시키되, 산화 탄화수소질 연료 원료공급원은 액체 탄화수소질 연료 또는 이들의 액체 에멀젼, 석유 코크스의 수성 슬러리, 또는 이들의 혼합물이고, 상기 연료는 할로겐화물, 알칼리금속 화합물, 황, 질소 및 무기 회분을 함유하는 성분을 포함하고 내화성 피복된 수직의 부분 산화 가스 발생기에서 유리 산소를 함유하는 기체와 반응하여 980 내지 1650℃의 온도를 가지는 H2, CO, CO2, H2O, CH4, NH3, HCN, HCl, HF, H2S, COS, N2, Ar을 함유하고 미립자 물질과 증기상 알칼리금속 화합물을 포함하는 고온의 원료 가스기류를 제조하고; (2) 가스 냉각영역에서 상기 단계(1)의 고온 원료 가스기류를 540 내지 700℃로 부분적으로 냉각하고; (3) 상기 단계(2)의 원료 가스기류로부터 미립자 물질을 분리하고; (4) 보충 알칼리금속 화합물을 단계(3)의 가공중의 가스기류에 주입하여 가공중의 가스기류 내에 존재하는 시안화수소 및 기체 상태의 할로겐화수소와 반응시키고; 이 가스기류를 약 430 내지 540℃로 냉각하고 얻어진 가스기류를 여과하여 할로겐화 알칼리금속과 시안화물, 잔여 알칼리금속 화합물, 및 잔여미립자 물질을 분리하고; (5) 냉각 및 여과된 상기 단계(4)의 가스기류를 황-제거 영역에서 황 반응성 산화물을 함유하는 혼합 금속 산화물 흡착제와 접촉시키는데, 상기에서 단계(4)의 냉각 및 여과된 가스기류중의 황을 함유하는 기체는 황 반응성 산화물을 함유하는 혼합 금속 산화물 흡착제와 반응하여 황화된 흡착제를 생성하고; 냉각 및 여과된 가스기류로부터 상기 황화된 흡착제 물질을 분리하여 미립자 물질, 알칼리금속 화합물, 할로겐화수소, 시안화수소, H2S, COS가 실질적으로 없는 적어도 540℃의 온도를 가지는 정제된 가스기류를 제조하는 것으로 이루어진 합성 가스, 환원 가스 또는 연료 가스를 제조하기 위한 부분 산화방법.
  2. 제1항에 있어서, 상기 액체 탄화수소질 연료는 액화 석유 가스, 석유 증류액 및 잔류물, 가솔린, 나프타, 케로신, 정제되지 않은 석유, 아스팔트, 가스 오일, 잔류 오일, 타르 모래 및 세일유, 코올 오일, 벤젠, 톨루엔 및 크실렌 분획물 등의 방향족 탄화수소, 코올 타르, 유동 촉매 크래킹 처리로부터의 순환 가스 오일, 코커 가스 오일의 퓨어퓨랄 추출물, 타이어 오일 또는 이들의 혼합물인 것임을 특징으로 하는 방법.
  3. 제1항 또는 제2항에 있어서, 상기 기체 탄화수소 연료는 메탄, 에탄, 프로판, 부탄, 펜탄, 천연 가스, 수성 가스, 코크스-오븐 가스, 정유 가스, 아세틸렌정제 가스, 에틸렌 오프-가스, 합성 가스, 또는 이들의 혼합물인 것임을 특징으로 하는 방법.
  4. 제1항 내지 제3항중 어느 하나의 항에 있어서, 단계(4)로부터 방출되는 가공중의 가스기류를 촉매 수성 가스 이동 반응영역을 통과시켜 이 가공중의 가스기류를 단계(5) 이전에 540 내지 680℃의 온도를 가열하여 단계를 특징으로 하는 방법.
  5. 제4항에 있어서, 보충수를 상기 수성 가스 이동 반응영역 이전에 가공중의 가스기류에 주입하는 단계를 특징으로 하는 방법.
  6. 제1항 내지 제3항중 어느 하나의 항에 있어서, 단계(4)로부터 방출되는 가공중의 가스기류를 촉매메탄화 반응영역을 통과시켜 이 가공중의 가스기류를 단계(5)이전에 540 내지 680℃의 온도로 가열하는 단계를 특징으로 하는 방법.
  7. 제1항 내지 제3항중 어느 하나의 항에 있어서, 단계(4)로부터 방출되는 가스 기류를 단계(5)이전에 간접 열교환방법에 의해 540 내지 680℃의 온도로 가열하는 단계를 특징으로 하는 방법.
  8. 제1항 내지 제7항중 어느 하나의 항에 있어서, 단계(5)에서 540 내지 680℃의 온도 및 단계(1)의 가스발생기에서 라인내의 통상의 압력강하가 더적은 압력하에서 단계(4)의 가스기류 중의 H2S 및 COS가 상기 황 반응성 혼합금속 산화물의 황 반응성 부분과 반응하는 것임을 특징으로 하는 방법.
  9. 제1항 내지 제8항중 어느 하나의 항에 있어서, 단계(2)와 (3)이 단계(1)의 고온의 원료 가스기류를 가스 냉각영역에서 800 내지 980℃로 부분적으로 냉각하고; 상기 부분적으로 냉각된 원료 가스기류로부터 포집된 미립자 물질을 분리하고; 가공중의 가스기류 내의 암모니아를 촉매적으로 불균등화하여 단계(4)로 이송하기 위한 실질적으로 NH3가 없는 가공중의 가스기류를 제조하는 것으로 이루어진 것임을 특징으로 하는 방법.
  10. 제9항에 있어서, 단계(5)에서의 황 반응성 산화물과의 접촉은 540 내지 680℃의 온도에서 실시되는 것임을 특징으로 하는 방법.
  11. 제9항 또는 제10항에 있어서, 상기 가스기류가 800 내지 980℃에서 니켈 불균등화 촉매와 접촉하는 동안 상기 NH3가 N2및 H2로 불균등화되는 것임을 특징으로 하는 방법.
  12. 제1항 내지 제11항중 어느 하나의 항에 있어서, 상기 탄화수소질 연료 연료공급원은 980 내지 1650℃의 온도 및 2 내지 300atm의 압력하에서 탄화수소질 연료에 대한 물의 중량비가 0.1 내지 5.0이고 0/C의 원자비가 0.7 내지 1.5로 상기 유리 산소를 함유하는 기체와 반응하는 것임을 특징으로 하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019940013701A 1993-06-17 1994-06-17 정제된고온가스제조를위한부분산화방법 KR100317107B1 (ko)

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