Shale gas and condensate to chemicals

Patent metadata

Field	Value
Publication number	US-11041127-B2
Application number	US-201816639215-A
Country	US
Kind code	B2
Filing date	Aug 10, 2018
Priority date	Aug 15, 2017
Publication date	Jun 22, 2021
Grant date	Jun 22, 2021

Abstract

Provided are systems and methods for obtaining ethylene and propylene products from, for example, shale gas and shale gas condensate feedstocks. These systems and method operate by utilizing a hydrocracker train to crack C4 and C5 hydrocarbons to a product stream of propane and ethane or using a hydrogenolysis train to process C4 and C5 hydrocarbons to a product stream of propane and ethane that is provided to a cracker for an efficient conversion to ethylene and propylene. The disclosed systems are configured to reduce the amount of offsite hydrogen needed and also provide product streams that include a well-defined set of products as compared to existing approaches.

First claim

What is claimed:

1. A method of producing alkene products from a feedstock, the method comprising:
separating the feedstock, with a first separation train, into a light feedstock fraction comprising C1-C5 alkanes and a heavy feedstock fraction comprising C6+ alkanes;
effecting a cyclization process, with a cyclization train, on the heavy feedstock fraction so as to give rise to one or more of least benzene, toluene, xylenes, one or more gasoline range products, and cyclization train hydrogen;
removing methane, with a demethanizing train, from the light feedstock fraction so as to give rise to a demethanized light feedstock fraction comprising C2-C5 alkanes;
separating, with a second separation train, the demethanized light feedstock fraction so as to separate C2 and C3 alkanes from C4 and C5 alkanes;
(i) cracking, with a hydrocracker train, C5 alkanes developed at the second separation train and, optionally C4 alkanes developed at the second separation train, so as to give rise to a hydrocracker product stream comprising C1-C3 alkanes and communicating at least some of the hydrocracker product stream comprising C1-C3 alkanes to the demethanizing train or
(ii) processing, with a hydrogenolysis train, C5 alkanes developed at the second separation train and, optionally C4 alkanes developed at the second separation train, so as to give rise to a hydrogenolysis product stream comprising C1-C3 alkanes and communicating at least some of the hydrogenolysis product stream comprising C1-C3 alkanes to the demethanizing train; and cracking, with an alkane cracker train, C2 and C3 alkanes separated at the second separation train so as to give rise to an alkene product stream comprising C2 and C3 alkenes; and

cracking, with an alkane cracker train, C2 and C3 alkanes separated at the second separation train so as to give rise to an alkene product stream comprising C2 and C3 alkenes.

2. The method of claim 1 , further comprising communicating at least some of the cyclization train hydrogen to the hydrocracker train.

3. The method of claim 1 , further comprising combusting at least some of the methane removed by the demethanizing train so as to supply heat to one or more of the first separation train, the cyclization train, the demethanizing train, the second separation train, and the alkane cracker train.

4. The method of claim 3 , wherein combusting the methane provides within about 10% of the heat utilized by one or more of the first separation train, the cyclization train, the demethanizing train, the second separation train, and the alkane cracker train.

5. The method of claim 1 , wherein the alkane cracker train is characterized as a gas cracker.

6. The method of claim 1 , further comprising communicating, to the hydrocracker train or to the hydrogenolysis train, whichever present, at least some of the gasoline range products from the cyclization train, and further comprising cracking or effecting hydrogenolysis on the gasoline range products to form methane and C2-C3 alkanes.

7. The method of claim 1 , further comprising effecting dehydrogenation and metathesis on C4 alkanes developed at the second separation train so as to give rise to one or both of C2 and C3 alkenes.

8. The method of claim 7 , further comprising communicating hydrogen evolved in the dehydrogenation, metathesis, or both, to the hydrocracker train or the hydrogenolysis train, whichever present.

9. The method of claim 7 , further comprising communicating, to the cyclization train, hexene evolved by the metathesis.

Assignees

• Sabic Global Technologies Bv

Inventors

• Fickel Dustin
• Conant Travis
• Nagaki Dick Alan
• Velasco Pelaez Raul

Classifications

• C10G69/06

  including at least one step of thermal cracking in the absence of hydrogen · CPC title

• C10G47/18

  the catalyst containing platinum group metals or compounds thereof · CPC title

• C10G69/14

  plural parallel stages only · CPC title

• C10G45/68 Primary

  Aromatisation of hydrocarbon oil fractions · CPC title

• C10G2400/20

  C2-C4 olefins · CPC title