公开(公告)号：US20150014217A1

公开(公告)日：2015-01-15

申请号：US14308893

申请日：2014-06-19

Applicant: Randolph J. Smiley ,  Ajit Bhaskar Dandekar ,  Ramanathan Sundararaman ,  Rustom Merwan Billimoria ,  Thomas Francis Degnan, JR.

Inventor： Randolph J. Smiley ,  Ajit Bhaskar Dandekar ,  Ramanathan Sundararaman ,  Rustom Merwan Billimoria ,  Thomas Francis Degnan, JR.

IPC: C10G65/12

CPC classification number: C10G65/12 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12

Abstract: Improved yields of fuels and/or lubricants from a resid or other heavy oil feed can be achieved using slurry hydroconversion to convert at least about 90 wt % of the feed. The converted portion of the feed can then be passed into one or more hydroprocessing stages. An initial processing stage can be a hydrotreatment stage for additional removal of contaminants and for passivation of high activity functional groups that may be created during slurry hydroconversion. The hydrotreatment effluent can then be fractionated to separate naphtha boiling range fractions from distillate fuel boiling range fractions and lubricant boiling range fractions. At least the lubricant boiling range fraction can then be hydrocracked to improve the viscosity properties. The hydrocracking effluent can also be dewaxed to improve the cold flow properties. The hydrocracked and/or dewaxed product can then be optionally hydrofinished.

Abstract translation: 可以使用浆料加氢转化来转化至少约90重量％的进料，从渣油或其他重油进料中提高燃料和/或润滑剂的产率。 然后将进料的转化部分进入一个或多个加氢处理阶段。 初始处理阶段可以是加氢处理阶段，用于额外去除污染物和钝化可能在浆料加氢转化过程中产生的高活性官能团。 然后可以将加氢处理流出物进行分馏，从馏出燃料沸点馏分和润滑剂沸程馏分中分离出石脑油沸程。 至少可以将润滑剂沸程级分进行加氢裂化以提高粘度特性。 加氢裂化流出物也可以脱蜡以改善冷流特性。 加氢裂化和/或脱蜡产物可以任选加氢处理。

公开(公告)号：US10035959B2

公开(公告)日：2018-07-31

申请号：US14308905

申请日：2014-06-19

Applicant: Ramanathan Sundararaman ,  Thomas Francis Degnan, Jr. ,  Rustom Merwan Billimoria ,  Natalie Ann Fassbender ,  Manuel A. Francisco ,  Anjaneya Sarma Kovvali ,  Randolph J. Smiley ,  John Peter Greeley ,  William Ernest Lewis ,  Roby Bearden, Jr.

Inventor： Ramanathan Sundararaman ,  Thomas Francis Degnan, Jr. ,  Rustom Merwan Billimoria ,  Natalie Ann Fassbender ,  Manuel A. Francisco ,  Anjaneya Sarma Kovvali ,  Randolph J. Smiley ,  John Peter Greeley ,  William Ernest Lewis ,  Roby Bearden, Jr.

IPC: C10G47/26 ,  C10G49/06 ,  C10G49/12 ,  C10G69/14 ,  C10G49/04 ,  C10G69/06 ,  C10G9/00

CPC classification number: C10G49/12 ,  C10G9/005 ,  C10G49/04 ,  C10G49/06 ,  C10G69/06 ,  C10G69/14

Abstract: Systems and methods are provided for slurry hydroconversion of a heavy oil feed, such as an atmospheric or vacuum resid. The systems and methods allow for slurry hydroconversion using catalysts with enhanced activity and/or catalysts that can be recycled as a side product from a complementary refinery process.

公开(公告)号：US09605218B2

公开(公告)日：2017-03-28

申请号：US14308893

申请日：2014-06-19

Applicant: Randolph J. Smiley ,  Ajit Bhaskar Dandekar ,  Ramanathan Sundararaman ,  Rustom Merwan Billimoria ,  Thomas Francis Degnan, Jr.

Inventor： Randolph J. Smiley ,  Ajit Bhaskar Dandekar ,  Ramanathan Sundararaman ,  Rustom Merwan Billimoria ,  Thomas Francis Degnan, Jr.

IPC: C10G65/12 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12

CPC classification number: C10G65/12 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12

Abstract: Improved yields of fuels and/or lubricants from a resid or other heavy oil feed can be achieved using slurry hydroconversion to convert at least about 90 wt % of the feed. The converted portion of the feed can then be passed into one or more hydroprocessing stages. An initial processing stage can be a hydrotreatment stage for additional removal of contaminants and for passivation of high activity functional groups that may be created during slurry hydroconversion. The hydrotreatment effluent can then be fractionated to separate naphtha boiling range fractions from distillate fuel boiling range fractions and lubricant boiling range fractions. At least the lubricant boiling range fraction can then be hydrocracked to improve the viscosity properties. The hydrocracking effluent can also be dewaxed to improve the cold flow properties. The hydrocracked and/or dewaxed product can then be optionally hydrofinished.

公开(公告)号：US09605217B2

公开(公告)日：2017-03-28

申请号：US14308912

申请日：2014-06-19

Applicant: Ramanathan Sundararaman ,  Thomas Francis Degnan, Jr. ,  Rustom Merwan Billimoria ,  Randolph J. Smiley

Inventor： Ramanathan Sundararaman ,  Thomas Francis Degnan, Jr. ,  Rustom Merwan Billimoria ,  Randolph J. Smiley

IPC: C10G65/02 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12 ,  C10G65/10 ,  C10G65/12

CPC classification number: C10G65/02 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12 ,  C10G65/10 ,  C10G65/12

Abstract: Systems and methods are provided for sequential slurry hydroconversion of heavy oil feedstocks. One or more low pressure slurry hydroconversion stages can be used to perform a majority of the conversion of a heavy oil feedstock. The bottoms from the low pressure stages can then be slurry hydroconverted in one or more high pressure stages to further convert the feedstock.

公开(公告)号：US09499752B2

公开(公告)日：2016-11-22

申请号：US14309002

申请日：2014-06-19

Applicant: Ramanathan Sundararaman ,  Thomas Francis Degnan, Jr. ,  Rustom Merwan Billimoria ,  Keith Wilson ,  Randolph J. Smiley ,  Jacob Johannes Thiart

Inventor： Ramanathan Sundararaman ,  Thomas Francis Degnan, Jr. ,  Rustom Merwan Billimoria ,  Keith Wilson ,  Randolph J. Smiley ,  Jacob Johannes Thiart

IPC: C10G65/02 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12 ,  C10G65/10 ,  C10G65/12 ,  B01J23/89 ,  C10G65/00 ,  C10G67/02 ,  C10G69/02 ,  B01J35/02

CPC classification number: C10G65/02 ,  B01J23/8906 ,  B01J23/8913 ,  B01J35/023 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12 ,  C10G65/10 ,  C10G65/12 ,  C10G2300/107 ,  C10G2300/301

Abstract: Systems and methods are provided for slurry hydroconversion of a heavy oil feed, such as an atmospheric or vacuum resid. The systems and methods allow for slurry hydroconversion using catalysts with enhanced activity. The catalysts with enhanced activity can be used in conjunction with demetallization catalysts or catalysts that can be recycled as a side product from a complementary refinery process.

Abstract translation: 提供了用于重油进料（例如大气压或真空渣油）的浆料加氢转化的系统和方法。 该系统和方法允许使用具有增强活性的催化剂进行浆料加氢转化。 具有增强活性的催化剂可与脱金属催化剂或催化剂结合使用，所述脱金属催化剂或催化剂可作为辅助炼油方法的副产物回收。

公开(公告)号：US20150021233A1

公开(公告)日：2015-01-22

申请号：US14308912

申请日：2014-06-19

Applicant: Ramanathan Sundararaman ,  Thomas Francis Degnan, JR. ,  Rustom Merwan Billimoria ,  Randolph J. Smiley

Inventor： Ramanathan Sundararaman ,  Thomas Francis Degnan, JR. ,  Rustom Merwan Billimoria ,  Randolph J. Smiley

IPC: C10G65/02

CPC classification number: C10G65/02 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12 ,  C10G65/10 ,  C10G65/12

Abstract: Systems and methods are provided for sequential slurry hydroconversion of heavy oil feedstocks. One or more low pressure slurry hydroconversion stages can be used to perform a majority of the conversion of a heavy oil feedstock. The bottoms from the low pressure stages can then be slurry hydroconverted in one or more high pressure stages to further convert the feedstock.

Abstract translation: 提供系统和方法用于重油原料的顺序淤浆加氢转化。 可以使用一个或多个低压浆料加氢转化阶段来执行重油原料的大部分转化。 然后来自低压级的塔底物可以在一个或多个高压阶段中进行浆料加氢转化，以进一步转化原料。

公开(公告)号：US20150014216A1

公开(公告)日：2015-01-15

申请号：US14309002

申请日：2014-06-19

Applicant: Ramanathan Sundararaman ,  Thomas Francis Degnan, JR. ,  Rustom Merwan Billimoria ,  Keith Wilson ,  Randolph J. Smiley ,  Jacob Johannes Thiart

Inventor： Ramanathan Sundararaman ,  Thomas Francis Degnan, JR. ,  Rustom Merwan Billimoria ,  Keith Wilson ,  Randolph J. Smiley ,  Jacob Johannes Thiart

IPC: C10G65/02

CPC classification number: C10G65/02 ,  B01J23/8906 ,  B01J23/8913 ,  B01J35/023 ,  C10G45/16 ,  C10G47/26 ,  C10G49/12 ,  C10G65/10 ,  C10G65/12 ,  C10G2300/107 ,  C10G2300/301

Abstract: Systems and methods are provided for slurry hydroconversion of a heavy oil feed, such as an atmospheric or vacuum resid. The systems and methods allow for slurry hydroconversion using catalysts with enhanced activity. The catalysts with enhanced activity can be used in conjunction with demetallization catalysts or catalysts that can be recycled as a side product from a complementary refinery process.

Abstract translation: 提供了用于重油进料（例如大气压或真空渣油）的浆料加氢转化的系统和方法。 该系统和方法允许使用具有增强活性的催化剂进行浆料加氢转化。 具有增强活性的催化剂可与脱金属催化剂或催化剂结合使用，所述脱金属催化剂或催化剂可作为辅助炼油方法的副产物回收。

公开(公告)号：US20140374314A1

公开(公告)日：2014-12-25

申请号：US14308905

申请日：2014-06-19

Applicant: Ramanathan SUNDARARAMAN ,  Thomas Francis DEGNAN, JR. ,  Rustom Merwan BILLIMORIA ,  Natalie Ann FASSBENDER ,  Manuel A. FRANCISCO ,  Anjaneya Sarma KOVVALI ,  Randolph J. SMILEY ,  John Peter GREELEY ,  William Ernest LEWIS ,  Roby BEARDEN, JR.

Inventor： Ramanathan SUNDARARAMAN ,  Thomas Francis DEGNAN, JR. ,  Rustom Merwan BILLIMORIA ,  Natalie Ann FASSBENDER ,  Manuel A. FRANCISCO ,  Anjaneya Sarma KOVVALI ,  Randolph J. SMILEY ,  John Peter GREELEY ,  William Ernest LEWIS ,  Roby BEARDEN, JR.

IPC: C10G49/12 ,  C10G49/06 ,  C10G69/14

CPC classification number: C10G49/12 ,  C10G9/005 ,  C10G49/04 ,  C10G49/06 ,  C10G69/06 ,  C10G69/14

Abstract: Systems and methods are provided for slurry hydroconversion of a heavy oil feed, such as an atmospheric or vacuum resid. The systems and methods allow for slurry hydroconversion using catalysts with enhanced activity and/or catalysts that can be recycled as a side product from a complementary refinery process.

Abstract translation: 提供了用于重油进料（例如大气压或真空渣油）的浆料加氢转化的系统和方法。 这些系统和方法允许使用具有增强活性的催化剂和/或催化剂进行浆料加氢转化，所述催化剂可以作为辅助炼油方法的副产物回收。