公开(公告)号：US20100166622A1

公开(公告)日：2010-07-01

申请号：US12722035

申请日：2010-03-11

Applicant: Mark P. Lapinski ,  Richard R. Rosin

Inventor： Mark P. Lapinski ,  Richard R. Rosin

IPC: B01J19/00

CPC classification number: B01D53/864 ,  B01D53/02 ,  B01D2251/202 ,  B01D2253/108 ,  B01D2255/1026 ,  B01D2255/20746 ,  B01D2255/20753 ,  B01D2256/16 ,  B01D2256/24 ,  B01D2257/502 ,  B01J23/96 ,  B01J38/10 ,  C10G35/06

Abstract: One exemplary embodiment can be a process for lowering an amount of carbon monoxide in a stream rich in hydrogen. The process can include passing the stream rich in hydrogen through a carbon monoxide removal zone to produce a product stream having no more than about 10 vppm carbon monoxide and communicating the product stream to a reduction zone receiving a catalyst comprising unreduced metal species.

Abstract translation: 一个示例性实施方案可以是用于降低富含氢气的一氧化碳的量的方法。 该方法可以包括使富含氢的物流通过一氧化碳去除区，以产生具有不超过约10vppm一氧化碳的产物流，并将产物流连通至含有未还原金属物质的催化剂的还原区。

公开(公告)号：US20100018900A1

公开(公告)日：2010-01-28

申请号：US12179542

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: C10G35/02

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 n-butane 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 can include introducing the combined stream to a reforming reaction zone. Typically, the combined stream has an n-butane: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正丁烷的流和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，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。 通常，组合物流的正丁烷：石脑油质量比为约0.10:1.00-约1.00:1.00。

公开(公告)号：US20090261018A1

公开(公告)日：2009-10-22

申请号：US12104482

申请日：2008-04-17

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

IPC: C10G35/04 ,  B01J8/02

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。

公开(公告)号：US6013598A

公开(公告)日：2000-01-11

申请号：US991221

申请日：1997-12-12

Applicant: Mark P. Lapinski ,  Kenneth L. Riley ,  Clyde L. Aldridge ,  Michele S. Touvelle

Inventor： Mark P. Lapinski ,  Kenneth L. Riley ,  Clyde L. Aldridge ,  Michele S. Touvelle

IPC: B01J23/882 ,  B01J35/00 ,  B01J35/10 ,  C10G45/08 ,  B01J23/28 ,  B01J23/75

CPC classification number: C10G45/08 ,  B01J23/882 ,  B01J35/10 ,  B01J35/002 ,  B01J35/1061 ,  C10G2400/02

Abstract: The present invention relates to catalysts for hydrodesulfurizing naphtha streams. The catalysts are comprised of a suitable support material, and about 1 to about 10 wt. % MoO.sub.3, about 0.1 to about 5 wt. % CoO supported on a suitable support material. They are also characterized as having an average medium pore diameter from about 60 .ANG. to 200 .ANG., a Co/Mo atomic ratio of about 0.1 to about 1.0, a MoO.sub.3 surface concentration of about 0.5.times.10.sup.-4 to about 3.0.times.10.sup.-4 g MoO.sub.3 /m.sup.2, and an average particle size of less than about 2.0 mm in diameter.

Abstract translation: 本发明涉及用于加氢脱硫石脑油流的催化剂。 催化剂由合适的载体材料组成，约1至约10wt。 ％MoO 3，约0.1至约5wt。 ％CoO支持在合适的支撑材料上。 它们的特征还在于具有平均中等孔径从约60至200，Co / Mo原子比为约0.1至约1.0，MoO 3表面浓度为约0.5×10 -4至约3.0×10 -4 g MoO 3 / m2，平均颗粒直径小于约2.0mm。