专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US4696732A Simultaneous hydrotreating and dewaxing of petroleum feedstocks 失效
标题翻译：石油原料的同时加氢处理和脱蜡
公开(公告)号：US4696732A
公开(公告)日：1987-09-29
申请号：US829729
申请日：1986-02-14
申请人： Philip J. Angevine , Yung F. Chu , Kenneth M. Mitchell , Stephen M. Oleck , Stuart S. Shih , Robert C. Wilson, Jr., deceased
发明人： Philip J. Angevine , Yung F. Chu , Kenneth M. Mitchell , Stephen M. Oleck , Stuart S. Shih , Robert C. Wilson, Jr., deceased
IPC分类号： B01J29/46 , B01J29/70 , B01J29/76 , B01J29/80 , C10G45/08 , C10G45/64 , C10G45/12 , C10G47/20
CPC分类号： C10G45/64 , B01J29/46 , B01J29/7615 , B01J29/7623 , B01J29/80 , B01J2229/26 , B01J2229/42 , B01J29/7007
摘要： A process for simultaneously hydrotreating and dewaxing petroleum fractions is described. The process utilizes a single catalyst system which includes a hydrotreating component impregnated on a controlled pore size base and at least two catalyst components selected from any of an intermediate pore zeolite, a large pore zeolite or Zeolite Beta, and a large pore non-zeolite catalyst.
摘要翻译：描述了同时加氢处理和脱蜡石油馏分的方法。该方法使用单一催化剂体系，其包括浸渍在受控孔径基体上的加氢处理组分和至少两种选自中孔分子筛，大孔沸石或沸石β中的任一种的催化剂组分和大孔非沸石催化剂。

2. 发明授权

US4612108A Hydrocracking process using zeolite beta 失效
标题翻译：使用β沸石的加氢裂化工艺
公开(公告)号：US4612108A
公开(公告)日：1986-09-16
申请号：US762187
申请日：1985-08-05
申请人： Philip J. Angevine , Kenneth M. Mitchell , Stephen M. Oleck , Stuart S. Shih
发明人： Philip J. Angevine , Kenneth M. Mitchell , Stephen M. Oleck , Stuart S. Shih
IPC分类号： C10G45/64 , B01J29/70 , B01J29/76 , C10G47/16 , C10G65/10
CPC分类号： C10G47/16 , B01J29/7007 , B01J29/7615 , C10G65/10 , B01J2229/26 , B01J2229/42
摘要： A hydrocracking process for feedstocks containing high boiling, waxy components uses a number of sequential beds of hydrocracking catalyst based on zeolite beta. The proportion of zeolite beta in the catalyst increases in sequence so that the final bed has the highest zeolite concentration. The dewaxing activity of the zeolite beta-containing catalysts is enhanced by the use of sequential beds in this manner. The pour point of the high boiling fraction is reduced, as well as that of the distillate product, permitting part of the high boiling fraction to be included in the distillate product, thereby increasing the useful distillate yield.
摘要翻译：含有高沸点蜡状组分的原料的加氢裂化方法使用了基于沸石β的多个连续的加氢裂化催化剂层。催化剂中β沸石的比例依次增加，使得最终床具有最高的沸石浓度。通过以这种方式使用顺序床，增强了含β沸石催化剂的脱蜡活性。高沸点馏分的倾点以及馏出物产物的倾点降低，允许部分高沸点馏分包含在馏出物产物中，从而增加有用的馏出物产率。

3. 发明授权

US4689312A Procedure for regenerating platinum containing zeolite catalyst compositions 失效
标题翻译：再生含铂沸石催化剂组合物的方法
公开(公告)号：US4689312A
公开(公告)日：1987-08-25
申请号：US843549
申请日：1986-03-25
申请人： Quang Ngoc Le , Stephen J. McCarthy , Kenneth M. Mitchell
发明人： Quang Ngoc Le , Stephen J. McCarthy , Kenneth M. Mitchell
IPC分类号： B01J29/90 , C10G47/14 , B01J29/38 , B01J23/94 , B01J23/96 , C10G47/12
CPC分类号： B01J29/90 , C10G47/14
摘要： An improved regeneration procedure is described for restoring the hydrogen chemisorption of aged platinum containing zeolite catalyst compositions. The process includes subjecting th catalyst to reactivation, followed by oxygen regeneration. After regeneration, in accordance with the invention, a platinum containing zeolite catalyst composition has a platinum dispersion, illustrated by H.sub.2 chemisorption, equivalent to fresh catalyst.
摘要翻译：描述了一种改进的再生方法，用于恢复老化的含铂沸石催化剂组合物的氢化学吸附。该方法包括使催化剂再活化，接着进行氧再生。在再生之后，根据本发明，含铂沸石催化剂组合物具有铂分散体，其通过H 2化学吸附说明，相当于新鲜的催化剂。

4. 发明授权

US4101596A Low pressure xylene isomerization 失效
标题翻译：低压二甲苯异构化
公开(公告)号：US4101596A
公开(公告)日：1978-07-18
申请号：US758214
申请日：1977-01-10
申请人： Kenneth M. Mitchell , John J. Wise
发明人： Kenneth M. Mitchell , John J. Wise
IPC分类号： B01J29/00 , C07B61/00 , C07C1/00 , C07C5/27 , C07C15/08 , C07C67/00
CPC分类号： C07C5/2737 , Y02P20/52 , Y10S208/02 , Y10S585/954
摘要： Long on-stream periods of low pressure, vapor phase isomerization of xylenes is achieved in a system having tolerance of ethyl benzene in the charge by using a zeolite catalyst such as zeolite ZSM-5 at partial pressure of eight carbon atom aromatics below 100 pounds per square inch and temperature of 500.degree. F. to 800.degree. F.
摘要翻译：通过使用沸石催化剂如沸石ZSM-5在8碳原子芳族化合物的分压低于100磅/分的系统中，在具有对电荷的乙苯耐受性的系统中实现长时间的二氧化碳气相异构化平方英寸，温度500°F至800°F

5. 发明授权

US4647368A Naphtha upgrading process 失效
标题翻译：石脑油升级过程
公开(公告)号：US4647368A
公开(公告)日：1987-03-03
申请号：US787565
申请日：1985-10-15
申请人： Mary P. McGuiness , Kenneth M. Mitchell , Robert A. Ware
发明人： Mary P. McGuiness , Kenneth M. Mitchell , Robert A. Ware
IPC分类号： C10G59/02 , C10G69/08
CPC分类号： C10G59/02
摘要： An upgrading process for paraffinic naphthas subjects a full range naphtha to hydrocracking over a zeolite beta hydrocracking catalyst to effect a selective, partial hydrocracking in which the higher molecular weight n-paraffinic components of the naphtha are hydrocracked preferentially to the lower molecular weight components with concurrent isomerization of n-paraffins to isoparaffins, to form a hydrocracked effluent which comprises isobutane, C.sub.5 to C.sub.7 paraffins and relatively higher boiling naphthenes and paraffins. The hydrocracked effluent is split to remove the isobutane and the C.sub.5 and C.sub.7 paraffins with the balance of the higher boiling components being used as a reformer feed. Removal of the C.sub.5 and C.sub.7 paraffins permits improved reformer operation with the production of a higher octane product. The isomerization of the paraffins which occurs in the hydrocracking step provides a C.sub.5 to C.sub.7 paraffinic fraction which is of relatively higher octane number because of the shift to isoparaffins, permitting this component to be used as a gasoline blending component.
摘要翻译：石蜡石脑油的升级过程使全程石脑油在沸石β加氢裂化催化剂上进行加氢裂化，以实现选择性部分加氢裂化，其中石脑油的较高分子量正链烷烃组分优先加氢裂化至较低分子量组分，同时并入正链烷烃异构化为异链烷烃，形成加氢裂化的流出物，其中包括异丁烷，C5至C7链烷烃和相对较高沸点的环烷烃和石蜡。将加氢裂化的流出物分离以除去异丁烷，将C5和C7链烷烃与高沸点组分的余量用作重整器进料。去除C5和C7链烷烃允许改进重整器操作，同时生产较高辛烷值的产品。在加氢裂化步骤中发生的链烷烃的异构化提供了由于转移到异链烷烃而具有相对较高辛烷值的C5至C7链烷烃馏分，允许该组分用作汽油调和组分。

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