METHOD FOR DRIVING MACHINES IN AN ETHYLENE PLANT STEAM GENERATION CIRCUIT, AND INTEGRATED ETHYLENE AND POWER PLANT SYSTEM

Abstract

Method for driving machines, in an ethylene plant steam generation circuit, the method including recovering heat as high pressure steam from a cracking furnace; providing said high pressure steam to at least one steam turbine, wherein the steam turbine is configured to drive a machine, such as a process compressor; condensing at least part of the high pressure steam in a condenser; pumping condensed steam as boiler feed water back to the cracking furnace.

Claims

1. Method for driving machines, in an ethylene plant steam generation circuit, the method including: recovering heat as high pressure steam from a cracking furnace; providing the high pressure steam to at least one steam turbine, wherein the steam turbine is configured to drive a machine; condensing at least part of the high pressure steam in a condenser; pumping condensed steam as boiler feed water back to the cracking furnace; wherein the method also includes: recovering heat as high pressure steam from a waste heat recovery boiler of a power plant circuit; providing at least part of the high pressure steam from the power plant circuit to the at least one steam turbine of the ethylene plant steam generation circuit; and wherein excess fuel from the cracking furnace of the ethylene plant steam generation circuit is provided to the waste heat recovery boiler of the power plant circuit for auxiliary firing.

2. Method according to claim 1, wherein the waste heat recovery boiler is provided with exhaust gas from at least one gas turbine of the power plant circuit.

3. Method according to claim 2, wherein excess fuel from the cracking furnace of the ethylene plant steam generation circuit is provided to the gas turbine of the power plant circuit for combustion.

4. Method according to claim 2, wherein the at least one gas turbine is configured to drive a machine of the ethylene plant steam generation circuit.

5. Method according to claim 1, further including: providing at least part of the high pressure steam from the waste heat recovery boiler of the power plant circuit to at least one steam turbine of the power plant circuit, wherein the steam turbine is configured to drive a generator for generating power; condensing at least part of the high pressure steam in a condenser of the power plant circuit; pumping said condensed steam as boiler feed water back to the waste heat recovery boiler.

6. Integrated ethylene and power plant system, comprising an ethylene plant steam generation circuit and a power plant circuit configured to generate electric power, wherein the ethylene plant steam generation circuit includes: a cracking furnace for converting a hydrocarbon feedstock into cracked gas, wherein the cracking furnace is configured to generate high pressure steam from boiler feed water; at least one steam turbine configured to be driven by said high pressure steam; at least one process compressor configured to be driven by the at least one steam turbine; at least one condenser configured to condense at least part of the high pressure steam; at least one pump configured to pump the condensed steam to the cracking furnace as boiler feed water; wherein the power plant circuit includes a waste heat recovery boiler configured to recover heat as high pressure steam, wherein the system further comprises a first connection between the ethylene plant steam generation circuit and the power plant circuit configured to lead at least part of the high pressure steam from the waste heat recovery boiler to the at least one steam turbine of the ethylene plant steam generation circuit to drive said at least one steam turbine; and wherein the integrated ethylene and power plant system, further comprises a second connection between the ethylene plant steam generation circuit and the power plant circuit configured to lead at least part of excess fuel from the ethylene plant steam generation circuit to at least one burner of the waste heat recovery boiler.

7. Integrated ethylene and power plant system according to claim 6, wherein the power plant circuit further includes at least one gas turbine, wherein the at least one gas turbine is connected to the waste heat recovery boiler such that exhaust gas from the at least one gas turbine is recovered by the waste heat recovery boiler.

8. Integrated ethylene and power plant system according to claim 7, further comprising a further connection between the ethylene plant steam generation circuit and the power plant circuit configured to lead at least part of excess fuel from the ethylene plant steam generation circuit to the at least one gas turbine for combustion.

9. Integrated ethylene and power plant system according to claim 7, wherein the ethylene plant steam generation circuit includes at least one process compressor which is configured to be driven directly by the at least one gas turbine of the power plant circuit.

10. Integrated ethylene and power plant system according to claim 6, wherein the power plant circuit further includes at least one steam turbine and at least one generator, wherein the circuit is configured to provide at least part of the high pressure steam from the waste heat recovery boiler to the at least one steam turbine of the power plant circuit, wherein the at least one steam turbine is configured to drive the at least one generator for generating power.

11. Integrated ethylene and power plant system according to claim 10, wherein the power plant circuit further includes a condenser configured to condense at least part of the high pressure steam, and a pump configured to pump said condensed steam as boiler feed water back to the waste heat recovery boiler.

12. Integrated ethylene and power plant system according to claim 6, wherein the cracking furnace is a high efficiency cracking furnace including a radiant section, a convection section and a cooling section, wherein the cooling section includes at least one transfer line exchanger configured to preheat feedstock before entry into the radiant section, and wherein a convection section comprises a boiler coil configured to generate saturated steam from flue gas, said boiler coil being preferably located in a bottom part of the convection section.

13. Method according to claim 3, wherein the at least one gas turbine is configured to drive a machine of the ethylene plant steam generation circuit.

14. Method according to claim 2, further including: providing at least part of the high pressure steam from the waste heat recovery boiler of the power plant circuit to at least one steam turbine of the power plant circuit, wherein the steam turbine is configured to drive a generator for generating power; condensing at least part of the high pressure steam in a condenser of the power plant circuit; pumping said condensed steam as boiler feed water back to the waste heat recovery boiler.

15. Method according to claim 3, further including: providing at least part of the high pressure steam from the waste heat recovery boiler of the power plant circuit to at least one steam turbine of the power plant circuit, wherein the steam turbine is configured to drive a generator for generating power; condensing at least part of the high pressure steam in a condenser of the power plant circuit; pumping said condensed steam as boiler feed water back to the waste heat recovery boiler.

16. Method according to claim 4, further including: providing at least part of the high pressure steam from the waste heat recovery boiler of the power plant circuit to at least one steam turbine of the power plant circuit, wherein the steam turbine is configured to drive a generator for generating power; condensing at least part of the high pressure steam in a condenser of the power plant circuit; pumping said condensed steam as boiler feed water back to the waste heat recovery boiler.

17. Integrated ethylene and power plant system according to claim 8, wherein the ethylene plant steam generation circuit includes at least one process compressor which is configured to be driven directly by the at least one gas turbine of the power plant circuit.

18. Integrated ethylene and power plant system according to claim 7, wherein the power plant circuit further includes at least one steam turbine and at least one generator, wherein the circuit is configured to provide at least part of the high pressure steam from the waste heat recovery boiler to the at least one steam turbine of the power plant circuit, wherein the at least one steam turbine is configured to drive the at least one generator for generating power.

19. Method according to claim 1, wherein the steam turbine is configured to drive a process compressor.

20. Method according to claim 2, wherein the at least one gas turbine is configured to drive a process compressor of the ethylene plant steam generation circuit.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0015] The present invention will be further elucidated with reference to figures of exemplary embodiments. Corresponding elements are designated with corresponding reference signs.

[0016] FIG. 1 shows a schematic representation of an ethylene plant steam generation circuit and a power plant circuit;

[0017] FIG. 2 shows a schematic representation of an integrated ethylene and power plant system according to the invention.

DETAILED DESCRIPTION

[0018] FIG. 1 shows a schematic representation of an ethylene plant steam generation circuit and a power plant circuit. The ethylene plant steam generation circuit 1 comprises a cracking furnace 3 for converting a hydrocarbon feedstock into cracked gas. The cracking furnace 3 is configured to generate high pressure steam 4 from boiler feed water 5. The steam generation circuit 1 also includes at least one steam turbine 6 configured to be driven by said high pressure steam 4, and at least one process compressor 7, such as a cracked gas compressor, a propylene refrigeration compressor, an ethylene refrigeration compressor or other compressors, configured to be driven by the at least one steam turbine 6. The steam generation circuit 1 further includes at least one condenser 8 configured to condense at least part of the high pressure steam 4, and at least one pump 9 configured to pump the condensed steam to the cracking furnace as boiler feed water. The condenser 8 may for example be a surface condenser operating under vacuum, or a medium-pressure condenser, or any other condenser known to the person skilled in the art. In case of a conventional cracking furnace, enough high pressure steam 4 can be produced for the steam turbine 6 to drive a machine, such as a process compressor. However, if the cracking furnace 3 is a low emission cracking furnace with a revised heat recovery scheme as disclosed and shown in EP 3 415 587, then the low emission cracking furnace cannot produce a sufficient amount of high pressure steam 4 as needed for the steam turbine 6 to drive the at least one compressor 7. One or more of such process compressors 7 of the ethylene plant may then need to be driven by an electric motor 10. Power to drive said electric motor 10 may then be provided by a power plant 2. A conventional power plant 2 may include at least one gas turbine 11 having a combustion chamber 12 with an air compressor 13. Air 14 may be fed via the air compressor 13 to the combustion chamber 12, to which also fuel gas 15 may be fed. Fuel gas 15 can be combusted in the pressurized combustion chamber 12 with a relatively high excess air content. Flue gas generated by said combustion can be let down to ambient pressure over blades of the turbine 11, for example a back-pressure turbine. Forces acting on these blades may be used to drive a generator 16 configured to generate electric power to drive electric machines, such as for example the electric motor 10 configured to drive a process compressor in the ethylene plant. Flue gas, or exhaust gas 17, including excess air content, can leave the gas turbine 11 with a relatively high temperature and may be sent to a waste heat recovery boiler 18. Said boiler 18 may include additional burners, in which fuel 19 may be fired to reduce the excess air and to raise the temperature of the exhaust gas 17. Heat recovered in the waste heat recovery boiler 18 can be used to generate high pressure steam 20, which steam is used to drive a steam turbine 21, for example a condensing steam turbine. Said steam turbine 21 can then drive a generator 22 to generate power, in parallel with the power generated by the generator 16 driven by the gas turbine 11. The power generated by the generator 22 driven by the steam turbine 21 can be sent into a power grid or may also be used to drive electric machines, such as the electric motor 10 of the ethylene power plant circuit. The steam may be condensed under vacuum in a condenser 23, for example a surface condenser of the steam turbine 21. The condensed steam may optionally be first fed to a deaerator preferably using a condensate pump, which step is not shown, and can then be sent back by a boiler feed water pump 24 to the waste heat recovery boiler 18 as boiler feed water 25 to close the power plant circuit.

[0019] FIG. 2 shows a schematic representation of an integrated ethylene and power plant system according to the invention. Such an integrated system comprises an ethylene plant steam generation circuit 1′ configured to generate high pressure steam 4 from boiler feed water 5 for driving at least one machine, such as a process compressor 7, and a power plant circuit 2′ configured to generate electric power. The ethylene plant steam generation circuit includes a cracking furnace 3, in particular a high efficiency cracking furnace, for converting a hydrocarbon feedstock into cracked gas. The cracking furnace 3 is configured to generate high pressure steam 4 from boiler feed water 5. The ethylene plant steam generation circuit further includes at least one steam turbine 6 configured to be driven by said high pressure steam 4, at least one process compressor 7 configured to be driven by the at least one steam turbine 6, at least one condenser 8, for example a medium pressure condenser or a condenser operating under vacuum, configured to condense at least part of the high pressure steam 4, and at least one pump 9 configured to pump the condensed steam to the cracking furnace 3 as boiler feed water 5, closing the loop. The power plant circuit 2′ includes a waste heat recovery boiler 18 configured to recover heat as high pressure steam 20. In an inventive way, the system further comprises a first connection 27 between the ethylene plant steam generation circuit 1′ and the power plant circuit 2′ configured to lead at least part of the high pressure steam 20 from the waste heat recovery boiler 18 to the at least one steam turbine 6 of the ethylene plant steam generation circuit 1 to drive said at least one steam turbine 6. In analogy to the power plant circuit 2 of FIG. 1, the power plant circuit 2′ of the integrated system can further include at least one steam turbine 21 and at least one generator 22. The circuit 2′ may be configured to provide at least part of the high pressure steam 20 from the waste heat recovery boiler 18 to the at least one steam turbine 21 of the power plant circuit 2′, and the at least one steam turbine 21 may be configured to drive the at least one generator 22 for generating power. The power plant circuit 2′ can further include a condenser 23 configured to condense at least part of the high pressure steam 20, and a pump 24 configured to pump said condensed steam as boiler feed water 25 back to the waste heat recovery boiler 18. The power plant circuit 2′ can further include at least one gas turbine 11, being connected to the waste heat recovery boiler 18 such that exhaust gas 17 from the at least one gas turbine 11 is recovered by the waste heat recovery boiler 18. In an inventive way, fuel for additional firing in the recovery boiler 18 to raise the temperature of the exhaust gas 17 can be provided via a second connection (not shown) between the ethylene plant steam generation circuit 1′ and the power plant circuit 2′ leading at least part of excess fuel 26 from the ethylene plant steam generation circuit 1′ to at least one burner of the waste heat recovery boiler 18. In particular, cracked gas exiting a high efficiency cracking furnace 3 of the ethylene plant steam generation circuit 1′ may still include fuel gas which can be separated from the cracked gas, for example by cryogenic distillation. Said excess fuel 26 from the ethylene plant circuit can then advantageously be provided to at least one burner of the waste heat recovery boiler 18. A further connection (not shown) between the ethylene plant steam generation circuit 1′ and the power plant circuit 2′ can be configured to lead at least part of excess fuel 26 from the ethylene plant steam generation circuit 1′ to the at least one gas turbine 11, in particular to the combustion chamber 12 of the gas turbine 11, for combustion. The ethylene plant steam generation circuit 1′ may further include at least one process compressor 7′ which is configured to be driven directly by the at least one gas turbine 11 of the power plant circuit 2′, in contrast to the at least one process compressor 7 in FIG. 1, which may be driven by a steam turbine 6 or by an electric motor 10.

[0020] The project leading to this application has received funding from the European Union Horizon H2020 Programme (H2020-SPIRE-2016) under grant agreement no 723706.

[0021] For the purpose of clarity and a concise description, features are described herein as part of the same or separate embodiments, however, it will be appreciated that the scope of the invention may include embodiments having combinations of all or some of the features described. It may be understood that the embodiments shown have the same or similar components, apart from where they are described as being different.

[0022] In the claims, any reference signs placed between parentheses shall not be construed as limiting the claim. The word ‘comprising’ does not exclude the presence of other features or steps than those listed in a claim. Furthermore, the words ‘a’ and ‘an’ shall not be construed as limited to ‘only one’, but instead are used to mean ‘at least one’, and do not exclude a plurality. The mere fact that certain measures are recited in mutually different claims does not indicate that a combination of these measures cannot be used to an advantage. Many variants will be apparent to the person skilled in the art. All variants are understood to be comprised within the scope of the invention defined in the following claims.

REFERENCES

[0023] 1., 1′ Ethylene plant steam generation circuit [0024] 2., 2′ Power plant circuit [0025] 3. Cracking furnace [0026] 4. High pressure steam [0027] 5. Boiler feed water [0028] 6. Steam turbine [0029] 7., 7′ Process compressor [0030] 8. Condenser [0031] 9. Pump [0032] 10. Electric motor [0033] 11. Gas turbine [0034] 12. Combustion chamber [0035] 13. Compressor [0036] 14. Air [0037] 15. Fuel [0038] 16. Generator [0039] 17. Exhaust gas [0040] 18. Waste heat recovery boiler [0041] 19. Fuel [0042] 20. High pressure steam [0043] 21. Steam turbine [0044] 22. Generator [0045] 23. Condenser [0046] 24. Pump [0047] 25. Boiler feed water [0048] 26. Excess fuel [0049] 27. First connection