Olefins production process
Abstract
The invention relates to a process for producing olefins from a feed stream containing hydrocarbons by pyrolytic cracking of the hydrocarbons in a cracker furnace, said process comprising: pre-heating the feed stream outside the cracker furnace; feeding the pre-heated feed stream to a tube in the convection section of the cracker furnace; further pre-heating the feed stream in the convection section; feeding the further pre-heated feed stream to a tube in the radiant section of the cracker furnace; pre-heating an oxygen containing stream; contacting the pre-heated oxygen containing stream with a fuel gas in a burner in the radiant section; and pyrolytic cracking the feed stream in the radiant section resulting in an effluent containing olefins.
Claims
exact text as granted — not AI-modified1 . A process for producing olefins from a feed stream containing hydrocarbons by pyrolytic cracking of the hydrocarbons in a cracker furnace, said process comprising:
pre-heating the feed stream outside the cracker furnace; feeding the pre-heated feed stream to a tube in the convection section of the cracker furnace; further pre-heating the feed stream in the convection section; feeding the further pre-heated feed stream to a tube in the radiant section of the cracker furnace; pre-heating an oxygen containing stream; contacting the pre-heated oxygen containing stream with a fuel gas in a burner in the radiant section; and pyrolytic cracking the feed stream in the radiant section resulting in an effluent containing olefins.
2 . The process according to claim 1 , wherein the feed stream containing hydrocarbons is pre-heated outside the cracker furnace to a temperature which is at least 75° C. and which is at most 550° C.
3 . The process according to claim 1 , wherein one or more of the following heat sources is or are used in pre-heating the feed stream containing hydrocarbons outside the cracker furnace through indirect heat exchange between the feed stream and such heat source or heat sources: (i) very high pressure steam having a pressure of from greater than 70 bara to 130 bara; (ii) high pressure steam having a pressure of from greater than 30 bara to 70 bara; (iii) medium pressure steam having a pressure of from greater than 10 bara to 30 bara; (iv) low pressure steam having a pressure of from greater than atmospheric pressure to 10 bara; and (v) another heat source having a temperature of from greater than 50° C. to 100° C.
4 . The process according to claim 1 , wherein the olefins-containing effluent from the radiant section is used to provide pressurized steam through indirect heat exchange, in a first transfer line exchanger, between said effluent from the radiant section and utility water, and at least a portion of the cracker effluent coming from the first transfer line exchanger is sent to a next transfer line exchanger arranged in series wherein at least a portion of the feed stream containing hydrocarbons is pre-heated by indirect heat exchange with said effluent from the first transfer line exchanger, and wherein a transfer line exchanger is a system which comprises one or more indirect heat exchangers.
5 . The process according to claim 1 , further comprising:
pre-heating utility water outside the cracker furnace; and generating pressurized steam from the pre-heated utility water through indirect heat exchange with effluent from the radiant section.
6 . The process according to claim 1 , wherein the oxygen containing stream is pre-heated to a temperature which is at least 70° C. and which is at most 550° C.
7 . The process according to claim 1 , wherein the oxygen containing stream is pre-heated inside the cracker furnace through indirect heat exchange between the oxygen containing stream and flue gas in the convection section.
8 . The process according to claim 1 , wherein the feed stream containing hydrocarbons is not pre-heated in the convection section of the cracker furnace before pre-heating the feed stream outside the cracker furnace.Join the waitlist — get patent alerts
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