Recovery and re-use of waste energy in industrial facilities

Patent metadata

Field	Value
Publication number	US-10767932-B2
Application number	US-201816180828-A
Country	US
Kind code	B2
Filing date	Nov 5, 2018
Priority date	Aug 24, 2015
Publication date	Sep 8, 2020
Grant date	Sep 8, 2020

Abstract

Configurations and related processing schemes of direct or indirect (or both) inter-plants 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) inter-plants 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 system implemented 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, each oil refining plant comprising a plurality of interconnected oil refining sub-systems, wherein a plurality of streams at respective temperatures flow between the plurality of oil refining sub-systems, the system comprising:
a hydrocracking plant stream, a low temperature shift (LTS) converter product stream and a diesel hydro-treating plant stream of a hydrocracking plant, a steam reforming hydrogen plant and a diesel hydro-treating plant, respectively, of the plurality of oil refining plants, the hydrocracking plant stream comprising at least one of a feed stream to a first reaction stage cold high pressure separator, a feed stream to a second reaction stage cold high pressure separator, a product stripper overhead stream, a diesel product stream, a kerosene pumparound stream, and a kerosene product stream;
a stream from a first oil refining plant of the plurality of oil refining plants, the first oil refining plant being different from the hydrocracking plant, the steam reforming hydrogen plant and the diesel hydro-treating plant, the first oil refining plant comprising a naphtha hydro-treating plant, a sour water stripper plant, an amine regeneration plant separation section, a sulfur recovery plant and a gas separation plant through which a gas separation plant stream comprising at least one of C2 to C4 flows; and
one or more heat exchangers configured to transfer heat from one or more of the hydrocracking plant stream, the low temperature shift (LTS) converter product stream and the diesel hydro-treating plant stream to the stream from the first oil refining plant.

2. The system of claim 1 , wherein the first oil refining plant comprises a naphtha hydro-treating plant, a sour water stripper plant, an amine regeneration plant separation section, a sulfur recovery plant and a gas separation plant.

3. The system claim 2 , wherein the one or more heat exchangers are configured to indirectly transfer heat from one or more of the hydrocracking plant stream, the low temperature shift (LTS) converter product stream and the diesel hydro-treating plant stream to the stream from the first oil refining plant.

4. The system of claim 3 , wherein the one or more heat exchangers are configured to indirectly transfer heat through a buffer fluid using one or more of the hydrocracking plant stream, the low temperature shift (LTS) converter product stream and the diesel hydro-treating plant stream.

5. The system of claim 4 , wherein the buffer fluid comprises at least one of oil or water.

6. The system of claim 4 , wherein the one or more heat exchangers are configured to indirectly transfer heat through the buffer fluid using one or more of the hydrocracking plant stream, the low temperature shift (LTS) converter product stream and the diesel hydro-treating plant stream, and the one or more heat exchangers comprise:
a first heat exchanger configured to heat a first buffer fluid stream using the diesel product stream in the hydrocracking plant;
a second heat exchanger configured to heat a second buffer fluid stream using the feed stream to the second reaction stage cold high pressure separator in the hydrocracking plant;
a third heat exchanger configured to heat a third buffer fluid stream using the feed stream to the first reaction stage cold high pressure separator in the hydrocracking plant;
a fourth heat exchanger configured to heat a fourth buffer fluid stream using the product stripper overhead stream in the hydrocracking plant;
a fifth heat exchanger configured to heat a fifth buffer fluid stream using the kerosene pumparound stream in the hydrocracking plant;
a sixth heat exchanger configured to heat a sixth buffer fluid stream using the kerosene product stream in the hydrocracking plant;
a seventh heat exchanger configured to heat a seventh buffer fluid stream using the low temperature shift converter product stream in the steam reforming hydrogen plant;
an eighth heat exchanger configured to heat an eight buffer fluid stream using a diesel stripper overhead stream in the diesel hydro-treating plant; and
a ninth heat exchanger configured to heat a ninth buffer fluid stream using a diesel stripper bottoms stream in the diesel hydro-treating plant.

7. The system of claim 6 , further comprising a combined heated buffer fluid comprising:
the heated first buffer fluid stream exiting the first heat exchanger;
the heated second buffer fluid stream exiting the second heat exchanger;
the heated third buffer fluid stream exiting the third heat exchanger;
the heated fourth buffer fluid stream exiting the fourth heat exchanger;
the heated fifth buffer fluid stream exiting the fifth heat exchanger;
the heated sixth buffer fluid stream exiting the sixth heat exchanger;
the heated seventh buffer fluid stream exiting the seventh heat exchanger;
the heated eight buffer fluid stream exiting the eighth heat exchanger; and
the heated ninth buffer fluid stream exiting the ninth heat exchanger.

8. The system of claim 7 , further comprising:
a tenth heat exchanger positioned in the naphtha hydro-treating plant, the tenth heat exchanger configured to heat a naphtha splitter bottoms stream in the naphtha hydro-treating plant using the combined heated buffer fluid;
an 11 th heat exchanger positioned in the sour water stripper plant, the 11 th heat exchanger configured to heat a sour water stripper bottoms stream in the sour water stripper plant using the combined heated buffer fluid;
a 12 th heat exchanger positioned in the sulfur recovery plant, the 12 th heat exchanger configured to heat an amine regenerator bottoms stream in the sulfur recovery plant using the combined heated buffer fluid;
a 13 th heat exchanger positioned in the amine regeneration plant separation section, the 13 th heat exchanger configured to heat an acid gas regenerator bottoms stream in the amine regeneration plant separation section using the combined heated buffer fluid; and
a 14 th heat exchanger positioned in the gas separation plant, the 14 th heat exchanger configured to heat a C3/C4 splitter bottoms stream in the gas separation plant using the combined heated buffer fluid, the 14 th heat exchanger configured to heat a de-ethanizer bottoms stream using the combined heated buffer fluid.

9. The system of claim 8 , wherein the first heat exchanger, the second heat exchanger, the third heat exchanger, the fourth heat exchanger, the fifth heat exchanger, the sixth heat exchanger, the seventh heat exchanger, the eighth heat exchanger and the ninth heat exchanger are fluidically coupled to each other in parallel.

10. The system of claim 9 , wherein the tenth heat exchanger is fluidically coupled in series with a combination of the first heat exchanger, the second heat exchanger, the third heat exchanger, the fourth heat exchanger, the fifth heat exchanger, the sixth heat exchanger, the seventh heat exchanger, the eighth heat exchanger and the ninth heat exchanger.

11. The system of claim 10 , wherein the tenth heat exchanger, 11 th heat exchanger, the 12 th heat exchanger, the 13 th heat exchanger, the 14 th heat exchanger and the 15 th heat exchanger are fluidically coupled to each other in series.

12. The system of claim 10 , wherein the combined heated buffer fluid from the naphtha hydro-treating plant is flowed to the sour water stripper plant, then to the sulfur recovery plant, then to the amine regeneration plant separation section, and then to the gas separation plant.

Assignees

• Saudi Arabian Oil Co

Inventors

• Noureldin Mahmoud Bahy Mahmoud
• Al Saed Hani Mohammed

Classifications

• F01K13/00

  General layout or general methods of operation of complete plants · CPC title

• C10G69/00 Primary

  Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process (C10G67/00 takes precedence) · CPC title

• C01B3/34 Primary

  by reaction of hydrocarbons with gasifying agents · CPC title

• C10G2300/4006

  Temperature · CPC title

• F01D17/145

  by means of valves, e.g. for steam turbines (valves in general F16K) · CPC title