Method and system for steamcracking

Patent metadata

Field	Value
Publication number	US-12552996-B2
Application number	US-202218548881-A
Country	US
Kind code	B2
Filing date	Mar 8, 2022
Priority date	Mar 10, 2021
Publication date	Feb 17, 2026
Grant date	Feb 17, 2026

Abstract

A method of steam cracking includes using a steam cracking arrangement that has a fired cracking furnace, a quench cooling train, and rotating equipment at least partly driven by electric energy. A process gas stream is passed through the furnace and the cooling train. A steam generation arrangement, operated in thermal association with the cracking arrangement, results in superheated high pressure steam at a first pressure level of 30 and 175 bar absolute pressure and at a first temperature level. No steam at a higher temperature level than the first is generated. The superheated high pressure steam is partially adiabatically and isenthalpically expanded to a second lower pressure level. The first temperature level is selected such that each intermediate temperature level reached at intermediate pressure levels of more than 20 bar during the adiabatic and isenthalpic expansion process is between 5 and 120 K above the dew point of steam.

First claim

The invention claimed is:

1 . A method of steam cracking, comprising:
providing a steam cracking arrangement, including:
one or more fired cracking furnaces;
one or more quench cooling trains; and
one or more compressors and/or pumps as rotating equipment, wherein the rotating equipment is at least partly driven by electric energy;
passing one or more process gas streams at least through the one or more fired cracking furnaces and the one or more quench cooling trains; operating one or more steam generation arrangements in thermal association with the one or more steam cracking arrangements; wherein:
operating the one or more steam generation arrangements results in at least superheated high pressure steam at a first pressure level between 30 and 175 bar absolute pressure and at a first temperature level;
no steam at a higher temperature level than the first temperature level is generated in the one or more steam generation arrangements;
the superheated high pressure steam at the first pressure level is at least in part adiabatically and isenthalpically expanded to a second pressure level below the first pressure level such that its temperature level is lowered to a second temperature level; and
the first temperature level is selected such that each intermediate temperature level reached at intermediate pressure levels of more than 20 bar during the adiabatic and isenthalpic expansion is between 5 and 120 K above the dew point of steam at the respective intermediate pressure level during the adiabatic and isenthalpic expansion.

2 . The method according to claim 1 , wherein the superheated high pressure steam at the first pressure level and at the first temperature level does not include steam generated from process water and/or only includes steam generated from boiler feed water, such that the superheated high pressure steam at the first pressure level and at the first temperature level is provided as high-purity superheated high pressure steam.

3 . The method according to claim 2 , wherein the one or more process streams, before being passed through the one or more fired cracking furnaces of the one or more steam cracking arrangements, or feed hydrocarbons and/or process steam used in generating the one or more process streams, is or are at least in part heated using heat withdrawn from the one or more process streams downstream of the one or more fired cracking furnaces of the of the one or more steam cracking arrangements.

4 . The method according to claim 3 , wherein the heat withdrawn from the one or more process streams downstream of the one or more fired cracking furnaces of the of the one or more steam cracking arrangements is at least in part withdrawn from the one or more process streams downstream of the one or more fired cracking furnaces of the of the one or more steam cracking arrangements in one or more direct feed-effluent heat exchangers.

5 . The method according to claim 3 , wherein the heat withdrawn from the one or more process streams downstream of the one or more fired cracking furnaces of the one or more steam cracking arrangements is at least in part transferred to steam which is thereafter used in heating the one or more process streams, before being passed through the one or more fired cracking furnaces of the one or more steam cracking arrangements, or to feed hydrocarbons and/or the process steam used in generating the one or more process streams.

6 . The method according to claim 5 , wherein no steam generated by the one or more steam generation arrangements is expanded in steam turbines delivering shaft powers of more than 1 MW.

7 . The method according to claim 1 , wherein combustion air used in firing the one or more fired cracking furnaces is preheated to a temperature level of 100 to 1000° C., which is varied during operation.

8 . The method according to claim 7 , wherein the said combustion air is at least partially preheated in one or more multistream heat exchangers outside the flue gas pathway of the one or more fired cracking furnaces, and at least partially performed by using saturated steam produced in the one or more steam generation arrangements.

9 . The method according to claim 8 , wherein the said combustion air is at least partially preheated in one or more multistream heat exchangers in the flue gas pathway, wherein, in between two combustion air preheating steps, heat from flue gas is used for other process purposes.

10 . The method according to claim 1 , wherein the steam cracking arrangement or at least one of the steam cracking arrangements is operated, in different operating modes, using differing total fuel gas consumption rates, while maintaining a constant total cracking product yield.

11 . The method according to claim 1 , wherein a fuel gas used in firing the one or more fired cracking furnaces is heated to a temperature level which is varied during operation.

12 . The method according to claim 11 , wherein the fuel gas used in firing the one or more fired cracking furnaces has a hydrogen content between 0 and 100 wt.-%.

13 . The method according to claim 12 , wherein the fuel gas used in firing the one or more fired cracking furnaces is at least in part be provided by an electrolysis or ammonia decomposition unit.

14 . A system for performing a method of steam cracking, the system comprising:
one or more steam cracking arrangements, each steam cracking arrangement including:
one or more fired cracking furnaces;
one or more quench cooling trains; and
one or more compressors and/or pumps as rotating equipment; and
one or more steam generation arrangements operable in thermal association with the one or more steam crack arrangements; wherein:
the system is configured to pass one or more process gas streams at least through the one or more fired cracking furnaces and the one or more quench cooling trains of the one or more steam cracking arrangements;
the system is configured to drive the rotating equipment at least partly by electric energy;
the one or more steam generation arrangements is or are configured to generate at least superheated high pressure steam at a first pressure level of 30 and 175 bar absolute pressure and at a first temperature level and no steam at a higher temperature level than the first temperature level;
means are provided which are configured to expand the superheated high pressure steam at the first pressure level at least in part adiabatically and isenthalpically to a second pressure level below the first pressure level of at least 20 bar absolute pressure such that its temperature level is lowered to a second temperature level; and
the system is configured to select the first temperature level such that each intermediate temperature level reached at intermediate pressure levels of more than 20 bar during the adiabatic and isenthalpic expansion process is between 5 and 120 K above the dew point of steam at the respective intermediate pressure level during the adiabatic and isenthalpic expansion.

15 . The method according to claim 1 , wherein the one or more process streams, before being passed through the one or more fired cracking furnaces of the one or more steam cracking arrangements, or feed hydrocarbons and/or process steam used in generating the one or more process streams, is or are at least in part heated using heat withdrawn from the one or more process streams downstream of the one or more fired cracking furnaces of the of the one or more steam cracking arrangements.

16 . The method according to claim 1 , wherein no steam generated by the one or more ste

Assignees

• Linde Gmbh

Inventors

• Horenz Michael
• Zellhuber Mathieu
• Stegemann Robert
• Schmidt Gunther

Classifications

• F22D1/003

  Feed-water heater systems (F22D1/325, F22D1/36 and F22D1/40 take precedence) · CPC title

• C10G2400/22

  Higher olefins · CPC title

• C10G2400/20

  C2-C4 olefins · CPC title

• F22B1/1838 Primary

  the hot gas being under a high pressure, e.g. in chemical installations · CPC title

• C10G9/36 Primary

  with heated gases or vapours · CPC title