专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

61. 发明授权

KR100958362B1 나프타 접촉 분해 촉매 및 방법 失效
标题翻译：催化裂化催化剂和工艺
公开(公告)号：KR100958362B1
公开(公告)日：2010-05-17
申请号：KR1020077023366
申请日：2005-03-11
申请人： 유오피 엘엘씨
发明人： 아브레바야,하임 , 아브도,수헤일페어스 , 패튼,로버트라일
IPC分类号： C10G11/05 , B01J29/65 , B01J21/12
CPC分类号： C10G11/05 , B01J29/65 , B01J29/70 , B01J29/7003 , B01J29/80 , B01J29/90 , B01J2229/126 , B01J2229/186 , B01J2229/42 , B01J2229/62 , C10G11/18 , C10G2300/1044 , C10G2300/4006 , C10G2300/807 , C10G2400/20
摘要： 본 방법은 작은 세공을 가진 촉매를 이용하여 경질 올레핀의 제조를 향상시키기 위해 개시된다. 상기 촉매는 한정된 길이의 채널과 함께 10원 고리를 갖는 분자체를 포함한다. 상기 분자체는 실리카 대 알루미나의 고비율을 가지며 분해 방법 중에 방향족의 생성을 제한하기 위해 크기를 맞춘 세공을 가진다.

62. 发明公开

KR1020100041802A 디젤 및 방향족 화합물의 제조 방법 有权
标题翻译：生产柴油和芳香化合物的方法
公开(公告)号：KR1020100041802A
公开(公告)日：2010-04-22
申请号：KR1020107002215
申请日：2007-07-06
申请人： 유오피 엘엘씨
发明人： 프레이스탠리제이. , 타칼바산트피.
IPC分类号： C07C4/26 , C07C5/22 , C07C15/08 , C10L1/08
CPC分类号： C07C6/126 , Y02P20/132 , C07C15/08
摘要： A process for the production of low sulfur diesel and aromatic compounds wherein C+ hydrocarbons are hydrocracked to produce low sulfur diesel and a naphtha boiling range stream which is transalkylated in an integrated transalkylation zone to produce xylene.
摘要翻译：一种生产低硫柴油和芳族化合物的方法，其中C +烃被加氢裂化以产生低硫柴油和在一体化烷基转移区中烷基转移以产生二甲苯的石脑油沸程流。

63. 发明公开

KR1020100017555A 전환이 증가된 방향족의 선택적 불균등화 방법 无效
标题翻译：选择性芳族化合物转化的过程与增加的转化
公开(公告)号：KR1020100017555A
公开(公告)日：2010-02-16
申请号：KR1020097025101
申请日：2007-05-05
申请人： 유오피 엘엘씨
发明人： 볼딩흐,에드윈피.
IPC分类号： C07C5/52 , C07C15/08
CPC分类号： C07C6/123 , Y02P20/52 , C07C15/08
摘要： An improved process is disclosed for the selective disproportionation of toluene. The process preferably uses a disproportionation catalyst comprising a pentasil type zeolite such as MFI that is bound with aluminum-phosphate. Running the process at a toluene conversion greater than 30 wt-% and at a hydrogen-to-hydrocarbon ratio less than 3.0, and especially a ratio of 0.1 to 1.0, improves the maximum yield of para-xylene. Periodic rejuvenation by increasing the hydrogen-to-hydrocarbon ratio removes some carbon deposits and restores catalyst activity. An inert diluent gas assists in selective pre-coking of the catalyst as well.
摘要翻译：公开了用于甲苯选择性歧化的改进方法。该方法优选使用包含五氮烷型沸石的歧化催化剂，例如与磷酸铝结合的MFI。以大于30重量％的甲苯转化率和低于3.0的氢 - 烃比，特别是0.1至1.0的比例运行该方法提高了对二甲苯的最大产率。通过提高氢与烃的比例来定期回复除去一些碳沉积物并恢复催化剂活性。惰性稀释气体也有助于催化剂的选择性预焦化。

64. 发明公开

KR1020100014309A 방향족 화합물의 생성을 위한 통합 장치 有权
标题翻译：一体化生产设备
公开(公告)号：KR1020100014309A
公开(公告)日：2010-02-10
申请号：KR1020097014344
申请日：2007-01-29
申请人： 유오피 엘엘씨
发明人： 설리번로렌스이 , 마허그레고리 , 햄데이비드에이
IPC分类号： C07B63/00 , C07C15/04 , C07C15/08 , C07C7/10
CPC分类号： C07C6/126 , C07C5/2708 , C07C5/2724 , C07C7/005 , C07C7/04 , C07C7/08 , C07C2529/74 , C07C15/08 , C07C15/02 , C07C15/04
摘要： Enabling a transalkylation process to handle both C10 alkylaromatics and unextracted toluene permits the following improvements to be realized. No longer extracting toluene allows a reformate-splitter column to be eliminated. The extraction unit (27) can be moved to the overhead of a benzene column and integrated together with the transalkylation unit (36) to reduce costs. No longer requiring a rigorous split between Cand Calkylaromatics allows a heavy aromatics column to be eliminated. Such an enabled transalkylation process requires stabilization of a transalkylation catalyst through the introduction of a metal function. These improvements result in an aromatics complex apparatus with savings on inside battery limits curve costs and an improvement on the return on investment in such a complex.
摘要翻译：实施烷基转移方法来处理C10烷基芳族化合物和未萃取的甲苯允许实现以下改进。不再提取甲苯可以消除重整分离柱。提取单元（27）可以移动到苯塔的塔顶并与烷基转移单元（36）集成在一起以降低成本。不再需要坎德C烷基芳烃之间的严格分裂，可以消除重芳烃柱。这种使能的烷基转移方法需要通过引入金属官能团来稳定烷基转移催化剂。这些改进导致了芳烃复合设备，其内部电池限制曲线成本节省，并且对这种复杂的投资回报率有所改善。

65. 发明公开

KR1020100014272A 베타 제올라이트를 이용한 선택적 수소화분해 방법 无效
标题翻译：选择性水解工艺使用BETA ZEOLITE
公开(公告)号：KR1020100014272A
公开(公告)日：2010-02-10
申请号：KR1020097012523
申请日：2007-01-12
申请人： 유오피 엘엘씨
发明人： 왕리
IPC分类号： C10G45/12 , C10G45/06 , C10G65/10
CPC分类号： B01J29/7615 , B01J21/12 , B01J29/7815 , B01J35/002 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C10G47/20 , C10G65/10 , C10G2300/202 , C10G2300/301 , C10G2300/70 , C10G2400/04
摘要： Increased yields of middle distillate products are obtained in a hydrocracking process by the use of a catalyst containing a beta zeolite. In embodiments, the beta zeolite has not been hydrothermally treated or has been hydrothermally treated at a relatively low temperature. In another embodiment, the catalyst contains a relatively low amount of beta zeolite.
摘要翻译：通过使用含有β沸石的催化剂在加氢裂化方法中获得中间馏分产物的产率提高。在实施方案中，β沸石尚未经过水热处理或在相对低的温度下进行了水热处理。在另一个实施方案中，催化剂含有相对低量的β沸石。

66. 发明公开

KR1020090102813A 촉매 합금 수소 센서 장치 및 방법 无效
标题翻译：催化合金氢传感器装置及工艺
公开(公告)号：KR1020090102813A
公开(公告)日：2009-09-30
申请号：KR1020097015207
申请日：2007-12-03
申请人： 유오피 엘엘씨
发明人： 갤로웨이더글라스비 , 홀트란달이 , 벌렌패트릭제이
IPC分类号： G01N27/00 , G01N7/00 , B01J19/00 , B01D53/14
CPC分类号： G01N33/005
摘要： A process for controlling a refinery or chemical process has been developed. The process comprises flowing a feed conduit (206) to a processing unit (222); operating on the feed stream to generate an effluent stream (242); flowing the effluent stream (242) away from the process unit; passing at least a portion of the feed stream or the effluent stream through a catalytic alloy hydrogen sensor (212) and generating a signal corresponding to the concentration of hydrogen present in either the feed stream or the effluent stream; passing the signal to a display unit; and adjusting an operating parameter (232) of the process in response to at least the signal generated by the catalytic alloy hydrogen sensor (212). The display unit may be part of a computer (230) which automatically adjusts an operating parameter. The catalytic alloy hydrogen sensor (212) may be a palladium-nickel catalytic alloy hydrogen sensor.
摘要翻译：已经开发了用于控制炼油或化学过程的方法。该过程包括使进料管道（206）流动到处理单元（222）; 在进料流上操作以产生流出物流（242）; 使流出物流（242）离开处理单元; 使至少一部分进料流或流出物流通过催化合金氢传感器（212）并产生对应于存在于进料流或流出物流中的氢气浓度的信号; 将信号传递到显示单元; 以及响应于至少由催化合金氢传感器（212）产生的信号来调整该过程的操作参数（232）。显示单元可以是自动调整操作参数的计算机（230）的一部分。催化合金氢传感器（212）可以是钯镍催化合金氢传感器。

67. 发明公开

KR1020090100450A 이중 구역 방향족 알킬화 방법 无效
标题翻译：双区芳香烷基化方法
公开(公告)号：KR1020090100450A
公开(公告)日：2009-09-23
申请号：KR1020097016760
申请日：2008-01-09
申请人： 유오피 엘엘씨
发明人： 슈미츠,로버트,제이.
IPC分类号： C07C2/66 , C07C7/148 , C07C15/085 , B01J29/70
CPC分类号： C07C2/66 , B01J29/70 , B01J29/7007 , B01J35/0006 , B01J37/0009 , B01J2229/42 , C07C2529/70 , Y02P20/52 , C07C7/148 , C07C15/085
摘要： A process for the catalytic alkylation of an aromatic substrate with an alkylating agent is disclosed that comprises contacting the aromatic substrate and the alkylating agent in sequential alkylation zones to obtain an alkylaromatic. The first catalyst comprises UZM-8 zeolite and the second catalyst comprises beta zeolite. The process is particularly well suited for the alkylation of benzene with propylene to produce cumene.
摘要翻译：公开了一种用烷基化剂催化烷基化芳族底物的方法，其包括使芳族底物和烷基化剂在顺序的烷基化区中接触以获得烷基芳族化合物。第一种催化剂包括UZM-8沸石，第二种催化剂包括β沸石。该方法特别适用于苯与丙烯的烷基化以产生枯烯。

68. 发明授权

KR100916624B1 큐멘 하이드로퍼옥사이드의 분해 有权
标题翻译：碳氢化合物的分解
公开(公告)号：KR100916624B1
公开(公告)日：2009-09-08
申请号：KR1020087006554
申请日：2006-08-15
申请人： 유오피 엘엘씨
发明人： 슈미트,로버트,제이. , 슐츠,러셀,씨. , 뷸렌,패트릭,제이. , 타가몰리라,콘스탄트,피. , 랭크턴,스티븐,피. , 피터슨,게리,에이. , 페티스,마이클,이.
IPC分类号： C07C37/08 , C07C45/53
CPC分类号： C07C37/08 , C07C1/20 , C07C45/53 , C07C2527/054 , C07C15/44 , C07C49/08 , C07C39/04
摘要： 큐멘 하이드로퍼옥사이드(CHP) 및 다이메틸페놀카비놀(DMPC)을 함유하는 큐멘 산화 생성물 혼합물(1)을 분해하여 페놀과 아세톤(26)을 생산하는 방법.
큐멘 하이드로퍼옥사이드, 페놀

69. 发明公开

KR1020090094035A 쿠멘 히드로퍼옥시드의 분해를 위한 고체 산 촉매 및 방법 无效
标题翻译：固体酸催化剂和分解氢氧化钙的方法
公开(公告)号：KR1020090094035A
公开(公告)日：2009-09-02
申请号：KR1020097014869
申请日：2007-12-21
申请人： 유오피 엘엘씨
发明人： 슈미트로버트제이 , 잔등-양 , 밀러래린엠 , 존슨제임스에이
IPC分类号： C07C37/08 , C07C39/04 , C07C45/53 , C07C49/08
CPC分类号： B01J29/40 , B01J29/06 , B01J29/082 , B01J29/7007 , B01J29/85 , B01J35/002 , B01J37/0009 , B01J37/0045 , B01J37/0221 , B01J37/0246 , B01J2229/36 , B01J2229/42 , C07C37/08 , C07C45/53 , C07C407/00 , C07C409/10 , Y02P20/52 , C07C49/08 , C07C39/04
摘要： The present invention provides a process for decomposing a cumene hydroperoxide to produce phenol and acetone including: (1) introducing a process stream (21) containing cumene hydroperoxide into a reaction vessel (40); (2) introducing into the reaction vessel (40) a catalyst stream containing catalyst particles, the catalyst particles having an inner core, an outer layer bonded to the inner core, the outer layer comprising an acidic material having an acidity level when measured by NH3-TPD of equal to or greater than 0.36 mmoles NH3 per gram catalyst at 150 to 550 C based on using a powder form of the acidic material; (3) contacting the process stream (21) with the catalyst particles to form a product stream; and (4) withdrawing a portion of the product stream from the reactor (40) and recovering phenol and acetone products.
摘要翻译：本发明提供了分解氢过氧化枯烯以生产苯酚和丙酮的方法，包括：（1）将含有氢过氧化枯烯的工艺流（21）引入反应容器（40）中; （2）将含有催化剂颗粒的催化剂流引入到反应容器（40）中，催化剂颗粒具有内核，外层结合到内芯，外层包含酸性水平，当用NH 3 -TPD等于或大于0.36毫摩尔NH 3每克催化剂在150至550℃下，基于使用粉末形式的酸性材料; （3）使工艺流（21）与催化剂颗粒接触以形成产物流; 和（4）从反应器（40）中取出一部分产物流并回收苯酚和丙酮产物。

70. 发明公开

KR1020090082438A 적은 중질물 제조량 및 낮은 벤젠 대 올레핀 비에서 고체 산 촉매 상 알킬벤젠을 제조하는 방법 有权
标题翻译：通过低浓度固体酸催化剂生产烷基苯酚的方法，用于烯烃比例和低海拔
公开(公告)号：KR1020090082438A
公开(公告)日：2009-07-30
申请号：KR1020097010864
申请日：2007-10-29
申请人： 유오피 엘엘씨
发明人： 라일리,마크지. , 잔,덩-양 , 숀,스티븐더블유.
IPC分类号： C07C2/66 , C07C15/113 , B01J29/08 , C07C15/00
CPC分类号： C07C2/66 , C07C2529/08 , C07C15/107
摘要： The alkylation of aromatic compound with acyclic mono-olefin is effected at low aromatic compound to mono-olefin ratios with reduced co-production of heavies. In the processes a small crystal, acidic FAU molecular sieve is used as a catalyst under alkylation conditions. This invention also relates to catalysts containing small crystal, acidic FAU molecular sieve and at least one other acidic catalytic component.
摘要翻译：芳族化合物与无环单烯烃的烷基化在低芳族化合物与单烯烃比率下进行，同时减少重质量的共同产生。在该方法中，在烷基化条件下使用小结晶酸性FAU分子筛作为催化剂。本发明还涉及含有小结晶，酸性FAU分子筛和至少一种其它酸性催化组分的催化剂。

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