公开(公告)号：US09133403B2

公开(公告)日：2015-09-15

申请号：US13760247

申请日：2013-02-06

Applicant: UOP LLC

Inventor： Beckay J. Mezza ,  Haiyan Wang ,  Christopher P. Nicholas ,  Alakananda Bhattacharyya ,  Brenna E. Huovie ,  Rajeswar R. Gattupalli

IPC: C10G55/02 ,  C10G55/04 ,  C10G67/04 ,  C10G21/18 ,  C10G47/00

CPC classification number: C10G67/04 ,  C10G21/18 ,  C10G47/00 ,  C10G55/04 ,  C10G2300/205 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08

Abstract: The invention involves a process for hydrocarbon conversion. The process can include providing a feed to a primary upgrading zone and then treating the product from the primary upgrading zone with a feed-immiscible ionic liquid to remove metal compounds.

Abstract translation: 本发明涉及烃转化方法。 该方法可以包括向初级升级区提供进料，然后用与原料不混溶的离子液体处理来自初级升级区的产物以除去金属化合物。

公开(公告)号：US09133402B2

公开(公告)日：2015-09-15

申请号：US13760146

申请日：2013-02-06

Applicant: UOP LLC

Inventor： Beckay J. Mezza ,  Haiyan Wang ,  Christopher P. Nicholas ,  Alakananda Bhattacharyya ,  Brenna E. Huovie ,  Rajeswar R. Gattupalli

IPC: C10G55/02 ,  C10G55/04 ,  C10G55/06 ,  C10G67/04 ,  C10G21/18 ,  C10G47/00

CPC classification number: C10G67/04 ,  C10G21/18 ,  C10G47/00 ,  C10G55/04 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08

Abstract: The invention involves a process for hydrocarbon conversion. The process can include providing a feed to a primary upgrading zone and then treating the product from the primary upgrading zone with a feed-immiscible ionic liquid to remove nitrogen compounds.

Abstract translation: 本发明涉及烃转化方法。 该方法可以包括向初级升级区提供进料，然后用与原料不混溶的离子液体处理来自初级改质区的产物以除去氮化合物。

公开(公告)号：US08999145B2

公开(公告)日：2015-04-07

申请号：US13652439

申请日：2012-10-15

Applicant: UOP LLC

Inventor： Lorenz J. Bauer ,  Maureen L. Bricker ,  Beckay J. Mezza ,  Alakananda Bhattacharyya

IPC: C10G47/02 ,  C10G47/04

CPC classification number: C10G47/02 ,  C10G47/04 ,  C10G47/26

Abstract: One exemplary embodiment can be a slurry hydrocracking process. The process can include providing one or more hydrocarbon compounds having an initial boiling point temperature of at least about 340° C., and a slurry catalyst to a slurry hydrocracking zone. The slurry catalyst may have about 32-about 50%, by weight, iron; about 3-about 14%, by weight, aluminum; no more than about 10%, by weight, sodium; and about 2-about 10%, by weight, calcium. Typically, all catalytic component percentages are as metal and based on the weight of the dried slurry catalyst.

Abstract translation: 一个示例性实施方案可以是浆料加氢裂化方法。 该方法可以包括提供一种或多种具有至少约340℃的初始沸点温度的烃化合物，以及将淤浆催化剂提供给浆料加氢裂化区。 浆料催化剂可以具有约32-约50重量％的铁; 约3-约14％（重量）的铝; 不超过约10重量％的钠; 和约2-约10重量％的钙。 通常，所有的催化组分百分数都是金属，并且基于干浆料催化剂的重量。

公开(公告)号：US20150093313A1

公开(公告)日：2015-04-02

申请号：US14042647

申请日：2013-09-30

Applicant: UOP LLC

Inventor： Erin M. Broderick ,  Alakananda Bhattacharyya ,  Beckay J. Mezza

IPC: B01D53/52 ,  C07C7/11

CPC classification number: B01D53/526 ,  B01D53/1468 ,  B01D53/1493 ,  B01D2252/30 ,  B01D2252/504 ,  C07C7/11 ,  C10L3/103 ,  Y02P20/542 ,  C07C9/04

Abstract: The invention comprises a process for removal of hydrogen sulfide from gaseous mixtures. The process involves the use of a mixture of a physical absorption solvent and an ionic liquid. The mixtures provided improved absorption of hydrogen sulfide, when compared to physical absorption solvents without the ionic liquid at low partial pressures of hydrogen sulfide. A regeneration cycle involving the addition of a solvent, such as water, is used to regenerate the mixture.

Abstract translation: 本发明包括从气体混合物中除去硫化氢的方法。 该方法包括使用物理吸收溶剂和离子液体的混合物。 与在硫化氢低分压下没有离子液体的物理吸收溶剂相比，混合物提供了改善的硫化氢吸收。 使用包括加入溶剂如水的再生循环来再生混合物。