Recovery and re-use of waste energy in industrial facilities

Patent metadata

Field	Value
Publication number	US-9845995-B2
Application number	US-201615242041-A
Country	US
Kind code	B2
Filing date	Aug 19, 2016
Priority date	Aug 24, 2015
Publication date	Dec 19, 2017
Grant date	Dec 19, 2017

Abstract

Configurations and related processing schemes of direct or indirect (or both) intra-plants and thermally coupled heating systems synthesized for grassroots medium grade crude oil semi-conversion refineries to increase energy efficiency from specific portions of low grade waste heat sources are described. Configurations and related processing schemes of direct or indirect (or both) intra-plants and thermally coupled heating systems synthesized for integrated medium grade crude oil semi-conversion refineries and aromatics complex for increasing energy efficiency from specific portions of low grade waste sources are also described.

First claim

The invention claimed is:

1. A method implemented in a crude oil refining facility, the method comprising:
in a crude oil refining facility comprising a plurality of oil refining plants, each oil refining plant configured to perform at least one oil refining process, wherein a plurality of streams at respective temperatures flow between the plurality of oil refining plants:
flowing multiple streams, each stream from a sub-unit of a plurality of aromatics plant sub-units included in an aromatics plant of the plurality of oil refining plants, to one or more heat exchangers, wherein a stream from the aromatics plant comprises at least one of benzene, toluene or xylene;
flowing a stream from a first oil refining plant of the plurality of oil refining plants, the first oil refining plant being different from the aromatics plant, to the one or more heat exchangers, wherein the one or more heat exchangers transfer heat from one or more of the multiple streams to the stream from the first oil refining plant; and
utilizing the stream from the first oil refining plant heated by one or more of the multiple streams in an oil refining process at the first oil refining plant,

wherein the one or more aromatics plant sub-units comprises an aromatics complex xylene products separation unit and an aromatics complex benzene extraction plant, and wherein the first oil refining plant comprises a sulfur recovery plant,
wherein a stream of the multiple streams comprises an raffinate overhead stream in the aromatics complex xylene products separation unit,
wherein the stream from the first oil refining plant comprises at least one of an amine regenerator bottoms stream in a sulfur recovery plant of the plurality of oil refining plants, a benzene column bottoms stream in an aromatics complex benzene extraction plant of the plurality of aromatics plant sub-units, or a raffinate splitter column bottoms stream in the aromatics complex benzene extraction plant.

2. The method of claim 1 , wherein heating the stream from the first oil refining plant comprises directly heating the stream from the first oil refining plant using the multiple streams from the plurality of aromatics plant sub-units.

3. The method of claim 2 , wherein directly heating the stream from the first oil refining plant comprises:
heating, in a first heat exchanger, the amine regenerator bottoms stream in the sulfur recovery plant of the plurality of oil refining plants using a first branch of the raffinate overhead stream;
heating, in a second heat exchanger, the benzene column bottoms stream in the aromatics complex benzene extraction plant of the plurality of aromatics plant sub-units using a second branch of the raffinate overhead stream;
heating, in a third heat exchanger, the raffinate splitter column bottoms stream in the aromatics complex benzene extraction plant using a third branch of the raffinate overhead stream;
flowing the heated amine regenerator bottoms stream to the sulfur recovery plant; and
flowing the heated benzene column bottoms stream and the heated raffinate splitter column bottoms stream to the aromatics plant.

4. The method of claim 3 , wherein the first heat exchanger, the second heat exchanger and the third heat exchanger are fluidically coupled to each other in parallel.

5. The method of claim 2 , wherein the plurality of aromatics plant sub-units comprises an aromatics complex xylene products separation unit and an aromatics complex benzene extraction plant, wherein the first oil refining plant comprises a sour water stripper plant in the crude oil facility and wherein directly heating the stream comprises:
heating, in a first heat exchanger, a sour water stripper bottom stream in the sour water stripper plant using a first branch of the raffinate overhead stream;
heating, in a second heat exchanger, a benzene column bottoms stream in the aromatics complex benzene extraction plant using a second branch of the raffinate overhead stream; and
heating, in a third heat exchanger, raffinate splitter column bottoms stream in the aromatics complex benzene extraction plant using a third branch of the raffinate overhead stream; and
flowing the heated sour water stripper bottom stream, the heated benzene column bottoms stream and the heated raffinate splitter column bottoms stream to the aromatics plant.

6. The method of claim 5 , wherein the first heat exchanger, the second heat exchanger and the third heat exchanger are fluidically coupled to each other in parallel.

7. The method of claim 1 , wherein heating the stream from the first oil refining plant comprises indirectly heating the stream from the first oil refining plant through a buffer fluid using the multiple streams from the plurality of aromatics plant sub-units.

8. The method of claim 7 , wherein the buffer fluid comprises at least one of oil or water.

9. The method of claim 7 , wherein indirectly heating the stream from the first oil refining plant using the multiple streams from the plurality of aromatics plant sub-units comprises:
heating, in a first heat exchanger, the buffer fluid using a raffinate overhead stream in the aromatics complex xylene products separation unit of the plurality of aromatics plant sub-units.

10. The method of claim 9 , further comprising:
flowing the heated buffer fluid to a collection header;
splitting the heated buffer fluid into a first branch, a second branch and a third branch of the heated buffer fluid;
flowing the first branch of the heated buffer fluid to a sulfur recovery plant;
heating, in a second heat exchanger, an amine regenerator bottoms stream in the sulfur recovery plant using the first branch of the heated buffer fluid;
flowing the second branch of the heated buffer fluid to an aromatics complex benzene extraction unit; and
heating, in a third heat exchanger, a benzene column bottoms stream in the aromatics complex benzene extraction unit using the second branch of the heated buffer fluid.

11. The method of claim 10 , wherein the first heat exchanger and the second heat exchanger are fluidically coupled to each other in series, wherein the first heat exchanger and the third heat exchanger are fluidically coupled to each other in series, wherein the second heat exchanger and the third heat exchanger are fluidically coupled to each other in parallel, wherein the first heat exchanger and the fourth heat exchanger are fluidically coupled to each other in series, wherein the fourth heat exchanger and a combination of the second heat exchanger and the third heat exchanger are fluidically coupled to each other in parallel.

12. The method of claim 10 , further comprising:
flowing the heated buffer fluid to an amine regeneration plant separation section; and
heating, in a second heat exchanger, an acid gas regenerator bottom stream in the amine regeneration plant separation section using the heated buffer fluid.

13. The method of claim 12 , wherein the first heat exchanger and the second heat exchanger are fluidically coupled to each other in series.

14. The method of claim 9 , further comprising:
flowing the heated buffer fluid to an aromatics complex benzene extraction unit; and
heating, in a third heat exchanger, a benzene column bottoms stream in the aromatics complex benzene extraction unit using the heated buffer fluid.

15. The method of claim 14 , further comprising:
splitting the heated buffer fluid exiting the third heat exchanger into a first branch and a second branch of the heated buffer fluid;
flowing the first branch of the heated buffer fluid to a sour water stripper plant;
heating, in a second heat exchange

Assignees

• Saudi Arabian Oil Co

Inventors

• Noureldin Mahmoud Bahy Mahmoud
• Al Saed Hani Mohammed

Classifications

• C01B3/34 Primary

  by reaction of hydrocarbons with gasifying agents · CPC title

• C01B2203/0227

  containing a catalytic reforming step · CPC title

• C01B2203/127

  Catalytic desulfurisation · CPC title

• C01B2203/043

  Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration · CPC title

• C01B2203/0283

  containing a CO-shift step, i.e. a water gas shift step · CPC title