Method and installation for the production of hydrocarbons

Patent metadata

Field	Value
Publication number	US-12365840-B2
Application number	US-202017786821-A
Country	US
Kind code	B2
Filing date	Dec 18, 2020
Priority date	Dec 19, 2019
Publication date	Jul 22, 2025
Grant date	Jul 22, 2025

Abstract

A process is disclosed for the production of hydrocarbons with removal of coke from a product stream. In a first mode, hydrocarbons and steam are subjected to steam cracking to obtain a cracked gas. The removal of coke from the steam is performed using a coke trap thus obtaining a coke-depleted cracking gas which is subjected to quench heat exchange in the first mode downstream of the coke trap, effecting cooling. Product stream is formed in the first operating mode using the cracked gas cooled in the quench heat exchange. The coke trap is emptied in a second mode using a stream extracted from a cracking furnace, bypassing the quench heat exchange, to obtain a coke stream. The coke stream in the second mode is passed to a coke collector.

First claim

The invention claimed is:

1. A process for removal of coke from a cracked gas stream in a steam cracking plant, the process comprising:
in a first operating mode:
steam cracking a feed containing hydrocarbons and steam in a cracking furnace to obtain a cracked gas stream comprising coke and hydrocarbons;
passing the cracked gas stream to a downstream coke trap to remove coke and obtain a coke-depleted cracked gas; and
subjecting the coke-depleted cracked gas to heat exchange downstream of the coke trap to obtain a product gas stream comprising hydrocarbons; and

in a second operating mode:
emptying the coke trap by passing a withdrawal stream comprising steam from the cracking furnace through the coke trap, forming a coke stream;
bypassing the quench heat exchange with the coke stream; and
passing the coke stream to a coke collecting device;

wherein:
the cracked gas, downstream from the steam cracking, is sent via a conduit in a first direction, around a bend, and in a second direction downstream of the bend;
an inlet of the coke trap is arranged downstream of the bend in the first direction and a fluid connection from the conduit to the inlet starts from the bend;
an outlet of the coke trap is arranged in the first direction; and
the first direction is a direction deviating from the vertical direction by at least 45°.

2. The process according to claim 1 , wherein:
the inlet of the coke trap is arranged upstream of the quench heat exchanger and is fluidly connected to a conduit carrying the withdrawal stream;
the outlet of the coke trap is fluidly connected by a conduit to the coke collecting device.

3. The process according to claim 2 , wherein, downstream of the quench heat exchanger, an outlet of a further coke trap is fluidly connected by a conduit to the coke collecting device.

4. The process according to claim 3 , wherein the conduit connecting the coke trap to the coke collecting device opens at a shallow angle, in the range of 40° to 50°, into the conduit connecting the further coke trap to the coke collecting device.

5. The process according to claim 2 , wherein the coke collecting device comprises one or more of a cyclone, a fire box and a flow brake.

6. The process according to claim 2 , wherein the steam cracking plant further comprises one or more devices selected from the group consisting of a steam generator, a feed mixer, a reaction vessel, a cracked gas cooler, and a primary quench heat exchanger.

7. The process according to claim 2 , wherein the first and the second direction enclose an angle in the range of 30° to 120°.

8. The process according to claim 7 , wherein the first and the second direction enclose an angle in the range of 80° to 100°.

9. The process according to claim 8 , wherein the first and the second direction enclose an angle of about 90°.

10. The process according to claim 4 , wherein the conduit connecting the coke trap to the coke collecting device opens at a shallow angle of about 45° into the conduit connecting the further coke trap to the coke collecting device.

11. A steam cracking plant for the production of hydrocarbons comprising a cracking furnace, a quench heat exchanger, a coke trap and a coke collecting device, wherein the steam cracking plant is configured to perform the process of claim 1 , and wherein:
the coke trap has an inlet and an outlet, wherein:
the inlet is arranged downstream of the cracking furnace and upstream of the quench heat exchanger and is fluidly connected to a conduit carrying a withdrawal stream generated in the cracking furnace from a feed fluid containing hydrocarbons and/or steam;
the outlet is fluidly connected to the coke collecting device, bypassing the quench heat exchanger;
in a first operating mode, the coke trap is adapted to retain coke particles from the withdrawal stream; and
in a second operating mode, the coke trap is adapted to eject the coke particles in the direction of the coke collecting device using the withdrawal stream to obtain a coke stream;

a conduit carrying the withdrawal stream runs from the cracking furnace in a first direction, has a bend, and runs downstream of the bend in a second direction;
the inlet of the coke trap is arranged downstream of the bend in the first direction and the fluid connection of the inlet to the conduit starts from the bend;
the outlet of the coke trap is arranged in the first direction; and
the first direction is a direction deviating from the vertical direction by at least 45°.

Assignees

• Linde Gmbh

Inventors

• Kaiser Christian
• Sanktjohanser Mario
• Ziegler Christian

Classifications

• C10G2400/20

  C2-C4 olefins · CPC title

• C10G2300/4037

  In-situ processes · CPC title

• C10G9/36

  with heated gases or vapours · CPC title

• C10G9/20

  Tube furnaces · CPC title

• C10G9/16 Primary

  Preventing or removing incrustation · CPC title