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公开(公告)号：US5961817A
公开(公告)日：1999-10-05
申请号：US729935
申请日：1996-10-15
Applicant: William A. Wachter , Stuart L. Soled , Nikos J. Maris , Mark P. Lapinski , Carol P. Fitzpatrick
Inventor： William A. Wachter , Stuart L. Soled , Nikos J. Maris , Mark P. Lapinski , Carol P. Fitzpatrick
CPC classification number: B01J29/08 , B01J29/06 , B01J29/084 , C10G11/05 , B01J2229/42
Abstract: A FCC catalyst having improved coke selectivity and greater catalyst strength, and a FCC process for converting hydrocarbon feedstocks to lower boiling products. The catalyst comprises a crystalline aluminosilicate zeolite, gibbsite, and a silica matrix prepared from at least one of a silica sol made by an ion-exchange process and an acidic silica sol prepared by mixing sodium silicate, an acid and an aluminum salt of an acid.
Abstract translation: 具有改善焦炭选择性和更高催化剂强度的FCC催化剂，以及用于将烃原料转化为较低沸点产物的FCC方法。 该催化剂包括结晶硅铝酸盐沸石，三水铝矿和二氧化硅基质，其由至少一种通过离子交换方法制备的硅溶胶和通过混合硅酸钠，酸和酸的铝盐制备的酸性二氧化硅溶胶 。
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公开(公告)号：US20120277508A1
公开(公告)日：2012-11-01
申请号：US13417203
申请日：2012-03-10
Applicant: Gregory J. Gajda , Mary Jo Wier , Mark P. Lapinski , David A. Wegerer , Kurt M. Vanden Bussche , Mark D. Moser
Inventor： Gregory J. Gajda , Mary Jo Wier , Mark P. Lapinski , David A. Wegerer , Kurt M. Vanden Bussche , Mark D. Moser
IPC: C07C4/00
CPC classification number: C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
Abstract: A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
Abstract translation: 提出了一种重整烃流的方法。 该方法包括将石脑油进料流分成至少两个进料流并将每个进料流通过分离重整器。 改性剂在不同条件下运行，以利用不同烃组分的反应性质的差异。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。
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公开(公告)号：US20120275974A1
公开(公告)日：2012-11-01
申请号：US13440527
申请日：2012-04-05
Applicant: Mark D. Moser , Clayton C. Sadler , Mark P. Lapinski , Kurt M. VandenBussche
Inventor： Mark D. Moser , Clayton C. Sadler , Mark P. Lapinski , Kurt M. VandenBussche
IPC: B01J19/00
CPC classification number: C01B3/26 , B01J8/008 , B01J8/0415 , B01J8/0492 , B01J8/0496 , B01J2208/00194 , B01J2208/0053 , B01J2219/024 , C01B2203/0277
Abstract: An apparatus for reforming a hydrocarbon stream is presented. The apparatus involves changing the design of reformers and associated equipment to allow for increasing the processing temperatures in the reformers and heaters. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking.
Abstract translation: 提出了一种用于重整烃流的装置。 该设备包括改变重整器和相关设备的设计，以允许提高重整器和加热器中的加工温度。 改造者在不同条件下运行，以利用平衡中的优点，但需要进行修改以防止增加热裂解并防止焦化增加。
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14.发明授权Adsorbing polynuclear aromatics from a reforming process using adsorbents containing iron 有权使用含铁吸附剂从重整过程中吸附多核芳烃公开(公告)号：US08262901B2
公开(公告)日：2012-09-11
申请号：US12701187
申请日：2010-02-05
Applicant: Manuela Serban , Mark P. Lapinski , Mark D. Moser
Inventor： Manuela Serban , Mark P. Lapinski , Mark D. Moser
CPC classification number: C10G25/003 , C10G61/06 , C10G2300/1044 , C10G2300/1096 , C10G2300/301 , C10G2300/305 , C10G2300/4018 , C10G2400/02
Abstract: An exemplary embodiment can be a process for removing one or more polynuclear aromatics from at least one reformate stream from a reforming zone. The PNAs may be removed using an adsorption zone. The adsorption zone can include first and second vessels each vessel containing an activated carbon adsorbent. Generally, the process includes passing the at least a portion of an effluent of the reforming zone through the first vessel containing a first activated carbon adsorbent wherein the first activated carbon adsorbent comprises iron.
Abstract translation: 示例性实施方案可以是从重整区从至少一种重整产物流中除去一种或多种多核芳烃的方法。 可以使用吸附区去除PNA。 吸附区可以包括第一和第二容器，每个容器含有活性炭吸附剂。 通常，该方法包括使重整区的流出物的至少一部分通过包含第一活性炭吸附剂的第一容器，其中第一活性炭吸附剂包含铁。
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15.发明申请公开(公告)号：US20100018901A1
公开(公告)日：2010-01-28
申请号：US12179552
申请日：2008-07-24
Applicant: Steven L. Krupa , Mark P. Lapinski , Clayton C. Sadler
Inventor： Steven L. Krupa , Mark P. Lapinski , Clayton C. Sadler
IPC: C10G35/00
CPC classification number: C10G35/04
Abstract: One exemplary embodiment can be a process for producing a reformate by combining a stream having an effective amount of methane and a stream having an effective amount of naphtha for reforming. Generally, the naphtha includes not less than about 95%, by weight, of one or more compounds having a boiling point of about 38-about 260° C. as determined by ASTM D86-07. Moreover, the process can include introducing the combined stream to a reforming reaction zone. Generally, the combined stream has a methane:naphtha mass ratio of about 0.03:1.00-about 0.10:1.00.
Abstract translation: 一个示例性实施方案可以是通过将具有有效量的甲烷的流与具有有效量的石脑油的流组合用于重整来生产重整产品的方法。 通常，石脑油包括按ASTM D86-07测定的一种或多种沸点为约38-约260℃的化合物的重量百分比不小于约95％。 此外，该方法可以包括将组合的流引入重整反应区。 一般来说，组合物流的甲烷：石脑油质量比为约0.03:1.00-约0.10:1.00。
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Patent Agency Ranking16.发明授权Catalytic cracking process with Y zeolite catalyst comprising silica binder containing silica gel 失效含有二氧化硅粘合剂的含有硅胶的Y沸石催化剂的催化裂化方法
公开(公告)号：US5788834A
公开(公告)日：1998-08-04
申请号：US684523
申请日：1996-07-19
Applicant: Mark P. Lapinski
Inventor： Mark P. Lapinski
CPC classification number: C10G11/05 , B01J29/084
Abstract: A catalytic cracking catalyst and catalytic cracking process for cracking the 650.degree. F.+ portion in a heavy feed to lighter products. The catalytic cracking catalyst contains a Y zeolite in a silica binder that is substantially free of catalytically active alumina. The silica binder contains silica gel as a component.
Abstract translation: 一种催化裂化催化剂和催化裂化方法，用于将重料中的650°F +部分裂化成较轻的产物。 催化裂化催化剂含有基本上不含催化活性氧化铝的二氧化硅粘合剂中的Y沸石。 二氧化硅粘合剂含有硅胶作为组分。
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17.发明授权公开(公告)号：US08753503B2
公开(公告)日：2014-06-17
申请号：US12179524
申请日：2008-07-24
Applicant: Steven L. Krupa , Mark P. Lapinski , Clayton C. Sadler
Inventor： Steven L. Krupa , Mark P. Lapinski , Clayton C. Sadler
IPC: C10G35/00
CPC classification number: C10G35/04
Abstract: One exemplary embodiment can be a process for producing a reformate by combining a stream having an effective amount of isopentane and a stream having an effective amount of naphtha for reforming. Generally, the naphtha has not less than about 95%, by weight, of one or more compounds having a boiling point of about 38-about 260° C. as determined by ASTM D86-07. The process may include introducing the combined stream to a reforming reaction zone. The combined stream can have an isopentane:naphtha mass ratio of about 0.10:1.00-about 1.00:1.00.
Abstract translation: 一个示例性实施方案可以是通过将具有有效量的异戊烷的物流和具有有效量的石脑油的物流混合以重整来生产重整产品的方法。 通常，根据ASTM D86-07测定，石脑油具有不小于约95重量％的一种或多种沸点为约38-约260℃的化合物。 该方法可以包括将组合的流引入重整反应区。 合并的流可以具有约0.10:1.00-约1.00:1.00的异戊烷：石脑油质量比。
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18.发明授权Process and system for the transfer of a metal catalyst component from one particle to another 有权金属催化剂组分从一个颗粒转移到另一个颗粒的方法和系统公开(公告)号：US08404105B2
公开(公告)日：2013-03-26
申请号：US13025631
申请日：2011-02-11
Applicant: Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Scheier , Simon R. Bare
Inventor： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Scheier , Simon R. Bare
IPC: C10G35/04
CPC classification number: C10G35/085 , C10G35/095 , C10G35/24
Abstract: One exemplary embodiment can be a process for facilitating a transfer of a metal catalyst component from at least one donor particle to at least one recipient particle in a catalytic naphtha reforming unit. The process can include transferring an effective amount of the metal catalyst component from the at least one donor particle to the at least one recipient particle under conditions to effect such transfer to improve a conversion of a hydrocarbon feed.
Abstract translation: 一个示例性实施方案可以是促进金属催化剂组分从催化石脑油重整单元中的至少一个供体颗粒转移至至少一个受体颗粒的方法。 该方法可以包括在有效量的金属催化剂组分从至少一个供体颗粒转移到至少一个受体颗粒的条件下进行这种转移以提高烃进料的转化率。
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19.发明申请Adsorbing Polynuclear Aromatics From a Reforming Process at Reaction Temperatures 有权在反应温度下从重整过程吸附多核芳烃公开(公告)号：US20110147265A1
公开(公告)日：2011-06-23
申请号：US12701264
申请日：2010-02-05
Applicant: Manuela Serban , Mark P. Lapinski , Mark D. Moser
Inventor： Manuela Serban , Mark P. Lapinski , Mark D. Moser
CPC classification number: C10G25/00 , C10G35/04 , C10G2300/1096 , C10G2300/201
Abstract: One exemplary embodiment can be a process for removing one or more polynuclear aromatics from at least one reformate stream from a reforming zone. The PNAs may be removed using an adsorption zone. The adsorption zone can include first and second vessels. Generally, the process includes passing the at least a portion of an effluent of the reforming zone through the first vessel containing a first activated carbon. The adsorption zone is operated at a temperature of at least 370° C.
Abstract translation: 一个示例性实施方案可以是从重整区从至少一种重整产物流中除去一种或多种多核芳烃的方法。 可以使用吸附区去除PNA。 吸附区可以包括第一和第二容器。 通常，该方法包括使重整区的流出物的至少一部分通过含有第一活性炭的第一容器。 吸附区在至少370℃的温度下运行
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20.发明申请Process and System for the Transfer of a Metal Catalyst Component from One Particle to Another 有权将金属催化剂组分从一种颗粒转移到另一种颗粒的方法和系统公开(公告)号：US20110136655A1
公开(公告)日：2011-06-09
申请号：US13025631
申请日：2011-02-11
Applicant: Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
Inventor： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
CPC classification number: C10G35/085 , C10G35/095 , C10G35/24
Abstract: One exemplary embodiment can be a process for facilitating a transfer of a metal catalyst component from at least one donor particle to at least one recipient particle in a catalytic naphtha reforming unit. The process can include transferring an effective amount of the metal catalyst component from the at least one donor particle to the at least one recipient particle under conditions to effect such transfer to improve a conversion of a hydrocarbon feed.
Abstract translation: 一个示例性实施方案可以是促进金属催化剂组分从催化石脑油重整单元中的至少一个供体颗粒转移至至少一个受体颗粒的方法。 该方法可以包括在有效量的金属催化剂组分从至少一个供体颗粒转移到至少一个受体颗粒的条件下进行这种转移以提高烃进料的转化率。
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