KR910015325A - 증류반응기용 촉매시스템 - Google Patents
증류반응기용 촉매시스템 Download PDFInfo
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- KR910015325A KR910015325A KR1019910002005A KR910002005A KR910015325A KR 910015325 A KR910015325 A KR 910015325A KR 1019910002005 A KR1019910002005 A KR 1019910002005A KR 910002005 A KR910002005 A KR 910002005A KR 910015325 A KR910015325 A KR 910015325A
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- 239000003054 catalyst Substances 0.000 title claims description 20
- 238000004821 distillation Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 claims 31
- 238000000034 method Methods 0.000 claims 21
- 238000006555 catalytic reaction Methods 0.000 claims 8
- 239000007791 liquid phase Substances 0.000 claims 7
- 239000012530 fluid Substances 0.000 claims 6
- 239000000463 material Substances 0.000 claims 3
- 239000012071 phase Substances 0.000 claims 3
- 238000006243 chemical reaction Methods 0.000 claims 2
- 230000001276 controlling effect Effects 0.000 claims 2
- 239000011949 solid catalyst Substances 0.000 claims 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000004508 fractional distillation Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
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Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명의 구조물을 보여주기 위해 부분 절단한 증류탑의 부분정면도, 제2도는 본 발명에 따른 촉매 강수관의 부분적인 측면 사시도, 제3도는 본 발명에서 이용하는 질량전달 층단(tray)의 평면도.
Claims (38)
- 분별증류 및 질량전달 영역을 제공하는 일정간격을 둔 다수의 평판과; 고정식 구조로서 촉매를 담기 위하여 상기의 평판사이에 연장된 촉매 반응영역인 다수의 용기로 구성되고 이 용기가 평판사이로 액체흐름을 전달하기 위한 기본 유동경로 역할을 하는 것을 특징으로 하며 탑형 반응기를 통과하는 유체흐름의 증류와 촉매반응을 동시 실행하기 위해 반응기속에 사용하는 구조물.
- 제1항에 있어서, 용기에 투과성 외벽이 설치된 것을 특징으로 하는 구조물.
- 제2항에 있어서, 용기외벽이 스크린 재료로된 것을 특징으로 하는 구조물.
- 제1항에 있어서, 평판에 용기를 수용할 수 있는 크기의 다수의 공동이 있어서 이 용기가 평판을 관통하여 연장되는 것을 특징으로 하는 구조물.
- 제4항에 있어서, 용기가 다수의 용기를 관통하는 연장하는 것을 특징으로 하는 구조물.
- 제5항에 있어서, 용기에 입상형 고체촉매를 충전하여 촉매 반응 영역을 형성하는 것을 특징으로 하는 구조물.
- 제1항에 있어서, 용기둘레에 상단 및 하단이 있는 고체 원통부가 설치되고 이 원통부는 용기와 일정간격을 두고 연결되어 원통부 하단에 유체가 채워질 수 있도록 하는 것을 특징으로 하는 구조물.
- 제1항에 있어서, 용기를 통해 낙하하는 액체의 유속을 늦추기 위한 간섭 구조물이 용기내부에 설치되어 있는 것을 특징으로 하는 구조물.
- 제1항에 있어서, 촉매를 담는 상기 내부에 개방지역을 제공하는 수단이 있어 여기에서 액체가 방사형으로 흘러 용기를 통과하는 것을 특징으로 하는 구조물.
- 제9항에 있어서, 개방지역과 통하는 개방형태이고 일정 간격을 두고 하향하는 액체 수거영역을 제공하는 수단이 있고 이 영역에서 액체를 방사형으로 전달하는 것을 특징으로 하는 구조물.
- 제10항에 있어서, 개방지역의 어느 위치에서 용기의 외벽에 대해 액체흐름을 전환하는 수단이 있는 것을 특징으로 하는 구조물.
- 제1l항에 있어서, 개방지역의 단면적 크기가 액체수거 영역의 크기보다 더큰 것을 특징으로 하는 구조물.
- 제11항에 있어서, 용기벽, 개방지역 제공수단 및 액체수거 영역 제공수단이 모두 망상재료(meshmateria1)로된 것인 구조물.
- 제13항에 있어서, 액체수거영역이 평판수단의 어느 위치에서 이 평판수단 하부의 어느위치까지 연장되는 것을 특징으로 하는 구조물.
- 제11항에 있어서, 액체 수거영역이 평판위의 어느 위치에서 시작되고 이보다 아래에 있는 또다른 평판의 어느위치까지 연장되는 것을 특징으로 하는 구조물.
- 일정간격을 둔 다수의 증류장치가 역시 다수의 촉매함유 용기와 함께 탑속에 연결되어 있고, 또한 이 촉매함유 용기속에 입상 촉매를 충전하여 촉매베드를 만들어서 그결과 증류장치내에 촉매영역과 별도의 증류영역이 형성되도록 하는 것을 특징으로 하며 입상촉매를 활용하는 증류공정을 수반한 반응탑 제조방법.
- 제16항에 있어서, 촉매를 충전하여 촉매베드가 다수의 증류 장치를 통하여 연속적으로 연장되는 것을 특징으로 하는 방법.
- 제16항에 있어서, 촉매영역내에 개방지역 제공수단을 제공하여 방사형으로 액체흐름이 개방지역속에 수용되도록 하는 것을 특징으로 하는 방법.
- 제18항에 있어서, 개방지역과 통하는 개방형태이고 일정 간격을 두고 하향하는 액체수거영역을 제공하는 수단이 있고 이 영역에서 액체를 방사형으로 전달하는 것을 특징으로 하는 방법.
- 제19항에 있어서, 개방지역의 어느 위치에서 용기의 외벽에 대해 액체흐름을 전환하는 수단이 있는 것을 특징으로 하는방법.
- 제20항에 있어서, 용기벽, 개방지역 제공수단과 또한 액체수거 영역 제공수단이 모두 망상재료로된 것인 방법.
- 제21항에 있어서, 액체수거영역이 평판수단의 어느 위치에서 이 평판수단 하부의 어느 위치까지 연장되는 것을 특징으로하는 방법.
- 제15항에 있어서, 액체수 거영역이 평판위의 어느 위치에서 시작되고 이보다 아래에 있는 또다른 평판의 어느위치까지 연장되는 것을 특징으로 하는 방법.
- 내부에 촉매를 충전하여 제한적으로 촉매반응영역이 형성된 용기와 서로 연결시킨 일정간격을 둔 다수의 증류장치를 갖춘탑(column)을 제공하고, 액체흐름을 공급하고 촉매반응영역에 통과시켜서 촉매반응을 실행하고, 기체흐름을 탑에 공급하고, 액체흐름 일부와 기체흐름을 증류장치에 보내어 질량전달이 일어나게 하고, 또한 촉매반응 및 증류결과로 나온 생성물을 반응기로 부터 분리하는 단계로 구성되며 촉매가 들어있는 탑형 반응기속에서 유체흐름의 증류 및 촉매반응을 동시실행하는 방법.
- 제24항에 있어서, 기체흐름 공급단계에서 액체흐름 일부를 증류 하는 것으로 된 방법.
- 제24항에 있어서, 하나이상의 용기가 다수의 증류장치를 관통하여 연장하도록된 탑을 특징으로 하는 방법.
- 제26항에 있어서, 촉매영역내에 개방지역 제공수단을 설치하여 액체흐름이 방사형으로 개방지역속에 수용되도록 하는 것을 특징으로 하는 방법.
- 제27항에 있어서, 개방지역과 통하는 개방형태이고 일정 간격을 두고 하향하는 액체수거영역을 제공하는 수단이 있고 이영역에서 액체를 방사형으로 전달하는 것을 특징으로 하는 방법.
- 제28항에 있어서, 개방지역의 어느 위치에서 용기의 외벽에 대해 액체흐름을 전환하는 수단이 있는것을 특징으로 하는 방법.
- 제29항에 있어서, 용기벽, 개방지역 제공수단과 또한 액체수거 영역 제공수단이 모두 망상재료로된 것인 방법.
- 제30항에 있어서, 액체수거영역이 평판수단의 어느 위치에서 이 평판수단 하부의 어느 위치까지 연장되는 것을 특징으로 하는 방법.
- 제29항에 있어서, 액체수거영역이 평판위의 어느 위치에서 시작되고 이보다 아래에 있는 또다른 평면의 어느위치까지 연장되는 것을 특징으로 하는 방법.
- 유체흐름을 탑에 공급하고; (i)다수의 질량 전달장치 사이에 연장된 입상고체 촉매베드와 유체흐름이 액체상을 접촉시켜 액체상 성분을 촉매화학적으로 반응시키고; (ii)동시에 액체상 일부를 증류시켜 기체상을 형성하고 또한; 기체상과 액체상을 질량전달장치에 보내어 액상 및 기체상간의 질량전달을 수행하고 또한; 촉매베드를 통과하여 질량전달창치로가는 액체상 흐름을 조절해서 계의 반응을 제어하는 단계를 특징으로 하며, 탑속에서 유체흐름의 촉매반응 및 증류작업을 동시 실행하는 방법.
- 제33항에 있어서, 촉매베드를 통과하는 액체상의 흐름 조절단계가 촉매베드에서 형성된 액체의 수위를 조절하는 단계인것을 특징으로 하는 방법.
- 제33항에 있어서, 촉매베드내에 개방지역을 제공하고 또한 액체를 방사형으로 베드에 통과시켜 상기의 개방지역에 보내는단계를 특징으로 하는 방법.
- 제35항에 있어서, 개방지역과 통하는 개방형태로서 일정간격으로 하향하는 액체 수거영역을 제공하고 또한 개방 지역에서나온 액체가 상기의 수거영역으로 들어가 모이고 이 액체는 다시 방사형으로 상기의 촉매베드를 통과하는 것으로된 방법.
- 제30항에 있어서, 유체흐름을 개방지역 주변으로 보내어 접근 하도록 하는 단계를 포함하는 방법.
- 제33항에 있어서, 질량전달장치가 다수의 단과 이 단에 액체를 수거하기 위한 수단으로 구성된 것을 특징으로 하는 방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US475,971 | 1990-02-06 | ||
US07/475,971 US5108550A (en) | 1990-02-06 | 1990-02-06 | Catalyst system for distillation reactor |
US475,941 | 1990-02-06 |
Publications (2)
Publication Number | Publication Date |
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KR910015325A true KR910015325A (ko) | 1991-09-30 |
KR950004328B1 KR950004328B1 (ko) | 1995-04-28 |
Family
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Application Number | Title | Priority Date | Filing Date |
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KR1019910002005A KR950004328B1 (ko) | 1990-02-06 | 1991-02-06 | 증류반응기용 촉매시스템 |
Country Status (8)
Country | Link |
---|---|
US (2) | US5108550A (ko) |
EP (1) | EP0441058A3 (ko) |
JP (1) | JPH04363132A (ko) |
KR (1) | KR950004328B1 (ko) |
AU (1) | AU635814B2 (ko) |
CA (1) | CA2033460A1 (ko) |
MX (1) | MX167866B (ko) |
NZ (1) | NZ237006A (ko) |
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-
1990
- 1990-02-06 US US07/475,971 patent/US5108550A/en not_active Expired - Fee Related
- 1990-12-27 EP EP19900314302 patent/EP0441058A3/en not_active Ceased
- 1990-12-31 CA CA002033460A patent/CA2033460A1/en not_active Abandoned
-
1991
- 1991-02-01 MX MX024399A patent/MX167866B/es unknown
- 1991-02-04 NZ NZ237006A patent/NZ237006A/xx unknown
- 1991-02-05 AU AU70258/91A patent/AU635814B2/en not_active Ceased
- 1991-02-06 KR KR1019910002005A patent/KR950004328B1/ko active IP Right Grant
- 1991-02-06 JP JP3014611A patent/JPH04363132A/ja active Pending
- 1991-10-11 US US07/775,010 patent/US5291989A/en not_active Expired - Fee Related
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Also Published As
Publication number | Publication date |
---|---|
EP0441058A3 (en) | 1991-09-18 |
KR950004328B1 (ko) | 1995-04-28 |
MX167866B (es) | 1993-04-19 |
JPH04363132A (ja) | 1992-12-16 |
US5108550A (en) | 1992-04-28 |
CA2033460A1 (en) | 1991-08-07 |
AU7025891A (en) | 1991-08-08 |
US5291989A (en) | 1994-03-08 |
AU635814B2 (en) | 1993-04-01 |
NZ237006A (en) | 1993-04-28 |
EP0441058A2 (en) | 1991-08-14 |
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