专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

21. 发明公开

KR1020100087308A 알킬벤젠 히드로과산화물의 제조 방법 有权
标题翻译：生产烷基苯酚氢过氧化物的方法
公开(公告)号：KR1020100087308A
公开(公告)日：2010-08-04
申请号：KR1020107009547
申请日：2008-10-28
申请人： 스미또모 가가꾸 가부시끼가이샤
发明人： 요시이마사유키
IPC分类号： C07C407/00 , C07C409/10 , C07C409/08
CPC分类号： C07C409/08 , C07C37/08 , C07C39/04 , C07C45/53 , C07C407/00 , C07C409/10 , C07C409/12 , Y02P20/582 , C07C49/08
摘要： A process for producing an alkylbenzene hydroperoxide from an alkylbenzene solution containing 0.01 to 10 mmol/kg of phenols by subjecting the solution to oxidation with an oxygen-containing gas, including allowing a compound represented by formula (I) to be present in the alkylbenzene solution: wherein R1, R2, R3, R4 and R5 independently represent a hydrogen atom, an alkyl group or an aryl group and may combine with each other to form a non-aromatic ring, the molar ratio of the compound represented by formula (I) to the phenols in the alkylbenzene solution being 0.4 mol/mol or higher; is advantageous in providing economical and high-yield production of an alkylbenzene hydroperoxide.

22. 发明授权

KR100973452B1 저 나트륨 절단 산물 有权
标题翻译： LOW SODIUM CLEAVAGE产品
公开(公告)号：KR100973452B1
公开(公告)日：2010-08-02
申请号：KR1020030071698
申请日：2003-10-15
申请人： 켈로그 브라운 앤드 루트 인코포레이티드
发明人： 윌크스시어도르로버트 , 밴더살마크손턴 , 로저스윌리엄프레데릭주니어
IPC分类号： C07C37/68
CPC分类号： C07C45/53 , C07C37/08 , C07C37/82 , C07C49/08 , C07C39/04
摘要： 페놀 제조 공정에서 세정된 절단 산물 (WCP)는 나트륨 이온을 제거하기 위해 처리된다. WCP 는 수소 형태로 양이온 교환 수지와 접촉한 후, 유리 염기 또는 수산화물 형태로 음이온 교환 수지와 접촉하여 나트륨 이온이 본질적으로 없는 WCP 를 생산한다. 양이온 및 음이온 교환 수지는 각각 산 및 부식제를 이용하여 재생된다. 처리는 신규 및 현존하는 페놀 공정의 생산성 및 품질을 개선한다.

23. 发明公开

KR1020100061790A 액상 수소화에 의한 이소프로판올의 제조 방법 有权
标题翻译：通过液相加氢生产ISO-丙二醇的方法
公开(公告)号：KR1020100061790A
公开(公告)日：2010-06-09
申请号：KR1020107002837
申请日：2008-10-01
申请人： 이네오스 페놀 게엠베하 운트 콤파니 카게
发明人： 본만,랄프 , 폼페츠키,워너 , 웨버,마르쿠스
IPC分类号： C07C29/145 , C07C31/10 , C07C29/80 , C07C39/04
CPC分类号： C07C29/145 , C07C37/08 , C07C45/53 , C07C407/00 , Y02P20/125 , C07C49/08 , C07C409/10 , C07C31/10 , C07C39/04
摘要： The present invention relates to a process for the production of iso-propanol by liquid phase hydrogenation of acetone to iso-propanol in at least two hydrogenation reaction stages, each reaction stage comprising a hydrogenation reaction zone, wherein the hydrogenation reaction product leaving the reaction zone of the first reaction stage contains unreacted acetone and a product stream comprising acetone and iso-propanol is transferred to the reaction zone of a subsequent reaction stage said product stream having at the inlet to the reaction zone of said subsequent reaction stage a temperature of 60 to 100°C, wherein the temperature of the product stream leaving the reaction zone of said subsequent reaction stage at the outlet from said reaction zone is at most 40°C higher than the temperature of the product stream entering said reaction zone at the inlet to said reaction zone and the temperature in said subsequent reaction zone does not exceed 125°C, to a process of purifying an iso-propanol raw product containing less than 1000 wppm acetone comprising subjecting the iso-propanol raw product to a distillation in a dividing wall distillation column to obtain purified iso-propanol and to an integrated process for the production of phenol employing the above hydrogenation process.
摘要翻译：本发明涉及通过在至少两个氢化反应阶段中将丙酮液相氢化为异丙醇来生产异丙醇的方法，每个反应阶段包括氢化反应区，其中离开反应区的氢化反应产物的第一反应阶段包含未反应的丙酮，并且将包含丙酮和异丙醇的产物流转移到随后反应阶段的反应区，所述产物流在所述后续反应阶段的反应区的入口处具有60至 100℃，其中离开来自所述反应区出口的所述后续反应阶段的反应区的产物流的温度比在所述反应区的入口处进入所述反应区的产物流的温度高至多40℃ 反应区域和所述后续反应区域中的温度不超过125℃ 包括含有小于1000wppm丙酮的异丙醇原料，包括使异丙醇原料在分隔壁蒸馏塔中进行蒸馏以获得纯化的异丙醇，以及使用上述氢化方法生产苯酚的一体化方法。

24. 发明授权

KR100937463B1 큐멘 하이드로퍼옥사이드의 분해 失效
标题翻译：碳氢化合物的分解
公开(公告)号：KR100937463B1
公开(公告)日：2010-01-19
申请号：KR1020087006013
申请日：2006-08-15
申请人： 유오피 엘엘씨
发明人： 슈미트로버트제이 , 슐츠러셀씨 , 불렌패트릭제이 , 타가모리라콘스탄테피 , 랭크톤스티브피 , 피터슨게리에이 , 페티스마이클이
IPC分类号： C07C37/08 , C07C45/00
CPC分类号： C07C37/08 , C07C1/20 , C07C45/53 , C07C2527/054 , C07C15/44 , C07C49/08 , C07C39/04
摘要： 큐멘 산화 혼합물(8)을 간접 열 교환 표면(3)을 포함하는 분해 용기(2)의 주입구 내로 도입시키는 것으로서, 여기서, 간접 열 교환 표면(3) 주위를 통과함으로써 큐멘 산화 생성 혼합물 및 순환 스트림이 혼합, 반응 및 냉각됨으로써, 큐멘 산화 생성 혼합물(1)을 분해하여 페놀과 아세톤(23)을 부산물의 생성을 감소시켜 제조하는 방법.
큐멘 산화 혼합물, 간접 열 교환 표면, 페놀, 아세톤, 큐멘 하이드로퍼옥사이드, 디메틸페닐카르비놀

25. 发明公开

KR1020070093140A 통합적 분리 및 제조 방법 无效
标题翻译：综合分离和制备过程
公开(公告)号：KR1020070093140A
公开(公告)日：2007-09-17
申请号：KR1020077017277
申请日：2005-12-27
申请人： 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이
发明人： 바위스,안드레 , 츄터,레슬리,앤드류 , 함센,제릿,얀 , 반데르하이드,에버트 , 메나드,장-프랑소와 , 멀더,도미니커스,프레데리커스 , 스피어링,우터
IPC分类号： B01D53/22 , B01D53/92 , C07C7/144 , C07C7/00
CPC分类号： B01D53/229 , B01D53/22 , B01D63/06 , B01D2313/42 , B01D2319/04 , C07C29/04 , C07C29/12 , C07C29/145 , C07C29/76 , C07C41/09 , C07C45/002 , Y02C10/10 , C07C49/08 , C07C49/10 , C07C31/10 , C07C31/12 , C07C31/202 , C07C31/205 , C07C43/13
摘要： Integrated separation and preparation process comprising a gas separation process wherein a first component is separated from a mixture of components by diffusion of the first component through a porous partition into a stream of sweeping component; and a preparation process wherein the sweeping component is used as feed. Separation unit and device for use in such a process and industrial set-up for use in such a process.
摘要翻译：一种综合分离和制备方法，包括气体分离方法，其中第一组分通过第一组分通过多孔隔板扩散成清扫组分流而与组分混合物分离; 以及其中清扫组分用作饲料的制备方法。用于这种过程的分离单元和设备以及用于这种过程的工业设置。

26. 发明公开

KR1020060117368A 안전성이 개선된 쿠멘 하이드로퍼옥사이드의 인-프로세스취급 방법 및 그 장치 失效
标题翻译：具有改进安全性的过氧化氢过氧化氢处理方法和装置
公开(公告)号：KR1020060117368A
公开(公告)日：2006-11-16
申请号：KR1020067017988
申请日：2005-01-06
申请人： 수노코, 인코포레이티드(알앤드엠)
发明人： 스킵워쓰제임스쥐. , 델라바제임스엠.
IPC分类号： C07C37/08 , C07C45/53
CPC分类号： C07C37/08 , B01J19/0013 , B01J2219/00081 , B01J2219/00085 , B01J2219/00777 , C07C45/53 , F28D7/06 , C07C49/08 , C07C39/04
摘要： The present invention provides a method and apparatus for in-process handling of concentrated cumene hydroperoxide ("CHP") in a process for the production of phenol and acetone by the decomposition of CHP. The method of the present invention makes use of a tube and shell type heat exchanger as a vessel to accumulate a working volume of concentrated CHP from a distillation unit. Concentrated CHP is then fed to a decomposer unit from the accumulated working volume. Use of a tube and shell type heat exchanger improves safety over designs that make use of an unmodified tank or drum.
摘要翻译：本发明提供了在通过CHP分解生产苯酚和丙酮的方法中过程处理浓缩的氢过氧化枯烯（“CHP”）的方法和装置。本发明的方法利用管壳型热交换器作为容器，从蒸馏单元积蓄浓缩CHP的工作容积。然后将浓缩的CHP从累积的工作容积送入分解器单元。使用管壳型热交换器提高了使用未经改装的罐或桶的设计的安全性。

27. 发明公开

KR1020050088178A 페놀, 아세톤, α-메틸스타이렌 및 프로필렌 옥사이드의동시 제조방법, 및 이를 위한 촉매 失效
标题翻译：苯酚，乙腈，α-甲基苯乙烯和丙烯氧化物及其催化剂的共生产
公开(公告)号：KR1020050088178A
公开(公告)日：2005-09-02
申请号：KR1020057010980
申请日：2003-12-16
申请人： 엑손모빌 케미칼 패턴츠 인코포레이티드
发明人： 레빈도론 , 산티스테반조스구아달루페 , 스미스모리스씨 , 바툴리제임스씨
IPC分类号： C07C37/08 , C07C45/53 , C07C15/44
CPC分类号： C07C409/10 , B01J23/75 , B01J27/1853 , B01J37/03 , C07C1/20 , C07C37/08 , C07C45/53 , C07C407/00 , C07C2521/06 , C07C2523/28 , C07C2527/054 , Y02P20/52 , C07C15/44 , C07C49/08 , C07C39/04
摘要： A process is disclosed for producing alpha-methylstyrene, acetone, and phenol wherein the amount of alpha- methylstyrene produced may be controlled by selectively converting a portion of the cumene hydroperoxide to dimethyl phenyl carbinol, the hydrated form of alpha-methylstyrene. The dimethyl phenyl carbinol thus produced will lead to increased production of alpha-methylstyrene upon dehydration in the acid cleavage unit of the phenol plant. By controlling the fraction of the cumene hydroperoxide reduced to dimethyl phenyl carbinol, the amount of alpha-methylstyrene produced in the plant can be continuously set to meet the demand of the market for alpha- methylstyrene. Also disclosed is a non-acidic catalyst for reduction of cumene hydroperoxide.
摘要翻译：公开了用于生产α-甲基苯乙烯，丙酮和苯酚的方法，其中所产生的α-甲基苯乙烯的量可以通过选择性地将一部分氢过氧化枯烯转化为二甲基苯甲醇（α-甲基苯乙烯的水合形式）来控制。这样生产的二甲基苯甲醇将导致苯酚装置的酸裂解装置脱水时α-甲基苯乙烯的生产增加。通过控制二氢苯甲醇降解的氢过氧化枯烯的分数，可以连续设定工厂生产的α-甲基苯乙烯的量，以满足α-甲基苯乙烯市场的需求。还公开了用于还原枯烯氢过氧化物的非酸性催化剂。

28. 发明公开

KR1020000057572A 큐멘으로 부터 페놀 및 아세톤 제조 방법 有权
标题翻译：用于从CUMOL生产酚醛和丙酮的改进方法
公开(公告)号：KR1020000057572A
公开(公告)日：2000-09-25
申请号：KR1019997005328
申请日：1997-12-10
申请人： 아이엘엘에이 인터내셔날 리미티드 , 페놀케미에 게엠베하 운트 체오.카게
发明人： 자코스란스키,블라드미르미카일로비치 , 바실리에바,이리나이바노바 , 그리아즈노프,안드레이콘스탄틴노비치 , 유리에프,우리니콜라에비치 , 반바르네펠트,하인리히 , 게르리히,오트 , 클라이네-보이만,미카엘 , 클라인로,베르너 , 미카리크,크리스티앙
IPC分类号： C07C39/04
CPC分类号： C07C409/10 , C07C37/08 , C07C45/53 , C07C407/00 , Y02P20/52 , C07C49/08 , C07C39/04
摘要： PURPOSE: Cumol is oxidized into technical cumol hydroperoxide (CHP) and the resulting CHP is catalyzed to prepare phenol and acetone. CONSTITUTION: A method for producing phenol and acetone is improved by oxidizing cumol into technical cumol hydroperoxide (CHP) through catalytic cleavage of the CHP. During caltalytic cleavage of the technical CHP, a molar ratio of phenol:acetone:cumol should be maintained to 1:1:(0.38-0.61). According to the method, the oxidation products are concentrated up to a cumul content ranging from 21 to 30 wt.% in the technical cumul hydroperoxide, the mixture being used for the catalytic cleavage.
摘要翻译：目的：将Cumol氧化成技术性的氢过氧化物（CHP），催化所得CHP制备苯酚和丙酮。构成：通过催化裂解CHP，将枯子氧化成技术性的氢过氧化氢（CHP），可以改善生产苯酚和丙酮的方法。在技术性CHP的血管切割过程中，苯酚：丙酮：cum摩尔的摩尔比应保持在1：1：（0.38-0.61）。根据该方法，氧化产物在技术性累积氢过氧化物中浓缩至浓度范围为21-30重量％，该混合物用于催化裂解。

29. 发明公开

KR1020000017066A 유기산 및/또는 무기산을 유기 상으로부터 제거하는 방법 无效
标题翻译：从有机相消除有机酸和/或无机酸的方法
公开(公告)号：KR1020000017066A
公开(公告)日：2000-03-25
申请号：KR1019990031943
申请日：1999-08-04
申请人： 이네오스 페놀 게엠베하 운트 콤파니 카게
发明人： 폼페쯔키베르너 , 게를리히옷토
IPC分类号： B01D11/04
CPC分类号： C07C45/80 , C07B63/00 , C07C45/53 , C07C45/79 , C07C49/08
摘要： PURPOSE: A method for eliminating an organic acid and/or an inorganic acid from an organic phase is provided to eliminate an organic acid and/or an inorganic acid from the generated degradation product phase when manufacturing phenol by resolving cumin hydroperoxide. CONSTITUTION: The organic acid and/or an inorganic acid is eliminated from the organic phase by the steps of: flowing a degradation product(2) to be processed from the lower part of an extractor(E) into the extractor; flowing water(1) from the upper part of the extractor into the extractor; flowing out the extracted acid(4) from the extractor on the foot of an extract unit; passing the acid-eliminated organic phase e(3) through an anion exchanger(A1) or a cation exchanger(A2) by obtaining it from the upper part of the extractor; feeding the relevant organic phase e(5) after passing the anion exchanger; and scrapping a salt-including aqueous phase e(7) which is formed when regenerating the anion exchanger.
摘要翻译：目的：提供从有机相中除去有机酸和/或无机酸的方法，通过分解孜然氢过氧化物制造苯酚时，从产生的降解产物相中除去有机酸和/或无机酸。构成：通过以下步骤从有机相中除去有机酸和/或无机酸：将待处理的降解产物（2）从萃取器（E）的下部流入萃取器; 流水（1）从提取器的上部进入提取器; 将提取的酸（4）从提取单元的底部的提取器流出; 通过从提取器的上部获得酸去除的有机相e（3）通过阴离子交换器（A1）或阳离子交换器（A2）; 在通过阴离子交换剂之后喂养有机相e（5）; 并且在再生阴离子交换剂时形成的含盐水相e（7）的报废。

30. 发明授权

KR1019950008274B1 방향족 히드록시 화합물과 카르보닐 화합물의 동시 제조방법 失效
标题翻译：生产同时芳香羟基和碳化合物的方法
公开(公告)号：KR1019950008274B1
公开(公告)日：1995-07-27
申请号：KR1019920702023
申请日：1991-12-25
申请人： 미쓰이도아쓰가가구가부시기가이샤
发明人： 마쓰다후지오 , 미야다카츠하루 , 가토다카조 , 스기야마에이치 , 이노우에가오루
IPC分类号： C07C27/10
CPC分类号： C07C45/36 , C07C27/10 , C07C37/58 , C07C41/26 , C07C45/28 , C07C45/34 , C07C45/35 , Y02P20/52 , C07C49/08 , C07C39/04 , C07C39/07 , C07C39/14 , C07C43/23

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式