Producing C5 olefins from steam cracker C5 feeds—a process using a catalytic distillation reactor system

Patent metadata

Field	Value
Publication number	US-10814302-B2
Application number	US-201916707197-A
Country	US
Kind code	B2
Filing date	Dec 9, 2019
Priority date	Jan 29, 2015
Publication date	Oct 27, 2020
Grant date	Oct 27, 2020

Abstract

Producing C5 olefins from steam cracker C5 feeds may include reacting a mixed hydrocarbon stream comprising cyclopentadiene, C5 olefins, and C6+ hydrocarbons in a dimerization reactor where cyclopentadiene is dimerized to dicyclopentadiene. The dimerization reactor effluent may be separated into a fraction comprising the C6+ hydrocarbons and dicyclopentadiene and a second fraction comprising C5 olefins and C5 dienes. The second fraction, a saturated hydrocarbon diluent stream, and hydrogen may be fed to a catalytic distillation reactor system for concurrently separating linear C5 olefins from saturated hydrocarbon diluent, cyclic C5 olefins, and C5 dienes contained in the second fraction and selectively hydrogenating C5 dienes. An overhead distillate including the linear C5 olefins and a bottoms product including cyclic C5 olefins are recovered from the catalytic distillation reactor system. Other aspects of the C5 olefin systems and processes, including catalyst configurations and control schemes, are also described.

First claim

What is claimed is:

1. A process for the selective hydrogenation of C5 dienes in a mixed C5 hydrocarbon stream, comprising:
feeding hydrogen and a C5-olefin containing stream comprising linear pentenes, dienes, acetylenes, and a diluent compound to a catalytic distillation reactor system;
concurrently in the catalytic distillation reactor system:
hydrogenating the acetylenes and dienes; and
fractionating the C5-olefin containing stream;

recovering an overheads fraction comprising the pentenes;
recovering a bottoms fraction;
wherein the catalytic distillation reactor system has at least three reaction zones, including:
a first reaction zone disposed below a C5-olefin containing stream feed elevation and containing a nickel-based hydrogenation catalyst;
a second reaction zone disposed above the C5-olefin containing stream feed elevation and containing a nickel-based hydrogenation catalyst; and
a third reaction zone disposed above the second reaction zone and containing a palladium-based hydrogenation catalyst;

purging a portion of the bottoms fraction;
reacting a remaining portion of the bottoms fraction in a total hydrogenation unit to convert cyclic C5 olefins to cyclopentane; and
recycling the cyclopentane to the catalytic distillation reactor system.

2. The process of claim 1 , wherein the nickel-based catalyst comprises from about 5 wt % to about 30 wt % nickel, wherein the nickel-based hydrogenation catalyst is disposed on a diatomaceous earth support, has a BET surface area in the range from about 20 m 2 /g to about 400 m 2 /g, and has a pore volume in the range from about 0.2 ml/g to about 0.7 ml/g, and wherein the palladium-based hydrogenation catalyst comprises from about 0.2 to about 1.0 wt % palladium disposed on an alumina support.

3. The process of claim 1 , further comprising feeding the overheads fraction from the catalytic distillation reactor system to a metathesis unit and converting the linear C5 olefins to propylene.

4. The process of claim 1 , further comprising separating the overheads fraction to recover a product fraction comprising linear C5 olefins and a recycle fraction comprising cyclopentene.

5. A process for the selective hydrogenation of C5 dienes in a mixed C5 hydrocarbon stream, comprising:
feeding hydrogen and a C5-olefin containing stream comprising linear pentenes, dienes, acetylenes, and a diluent compound to a catalytic distillation reactor system;
concurrently in the catalytic distillation reactor system:
hydrogenating the acetylenes and dienes; and
fractionating the C5-olefin containing stream;

recovering an overheads fraction comprising the pentenes;
recovering a bottoms fraction;
wherein the catalytic distillation reactor system has at least three reaction zones, including:
a first reaction zone disposed below a C5-olefin containing stream feed elevation and containing a nickel-based hydrogenation catalyst;
a second reaction zone disposed above the C5-olefin containing stream feed elevation and containing a nickel-based hydrogenation catalyst; and
a third reaction zone disposed above the second reaction zone and containing a palladium-based hydrogenation catalyst,
wherein the nickel-based catalyst comprises from about 5 wt % to about 30 wt % nickel, wherein the nickel-based hydrogenation catalyst is disposed on a diatomaceous earth support, has a BET surface area in the range from about 20 m 2 /g to about 400 m 2 /g, and has a pore volume in the range from about 0.2 ml/g to about 0.7 ml/g, and wherein the palladium-based hydrogenation catalyst comprises from about 0.2 to about 1.0 wt % palladium disposed on an alumina support.

6. The process of claim 5 , further comprising feeding the overheads fraction from the catalytic distillation reactor system to a metathesis unit and converting the linear C5 olefins to propylene.

7. The process of claim 5 , further comprising separating the overheads fraction to recover a product fraction comprising linear C5 olefins and a recycle fraction comprising cyclopentene.

Assignees

• Lummus Technology Inc

Inventors

• Xu Yongqiang
• Loezos Peter
• Groten Willibrord A
• Lemoine Romain

Classifications

• C10G50/00

  Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation · CPC title

• C10G45/40

  containing platinum group metals or compounds thereof · CPC title

• C10G45/36

  containing nickel or cobalt metal, or compounds thereof · CPC title

• C10G45/32

  Selective hydrogenation of the diolefin or acetylene compounds · CPC title

• C10G9/36

  with heated gases or vapours · CPC title