초록 ▼

A method and system are disclosed for co-production of olefins and electric power. The method includes determining a separation level, separating a hydrocarbon feed into a light fraction stream and a heavy fraction stream based on the determined separation level; generating electric power from the h

A method and system are disclosed for co-production of olefins and electric power. The method includes determining a separation level, separating a hydrocarbon feed into a light fraction stream and a heavy fraction stream based on the determined separation level; generating electric power from the heavy fraction stream; and cracking the light fraction stream in a pyrolysis unit to produce an effluent comprising olefins. The separation level may be based on olefin production requirements and electric power requirements or specific split of the hydrocarbon feed to be utilized for power generation and olefin production.

대표청구항 ▼

1. A hydrocarbon processing system comprising: a separation unit configured to divide a hydrocarbon feed into a light fraction stream and a heavy fraction stream;a process control unit having one or more control units and configured to adjust a separation level in the separation unit based on olefin

1. A hydrocarbon processing system comprising: a separation unit configured to divide a hydrocarbon feed into a light fraction stream and a heavy fraction stream;a process control unit having one or more control units and configured to adjust a separation level in the separation unit based on olefin production requirements and electric power requirements;a pyrolysis unit in fluid communication with the separation unit, wherein the pyrolysis unit is configured to create an olefin effluent from a portion of the light fraction stream; anda fuel conversion unit in fluid communication with the separation unit and configured to convert a portion of the heavy fraction stream into a turbine feed; anda turbine in fluid communication with the fuel conversion unit and configured to generate electric power with at least a portion of the turbine feed. 2. The system of claim 1, wherein a convection section of the pyrolysis unit is configured to heat the hydrocarbon feed prior to the separation unit dividing the hydrocarbon feed into the light stream and the heavy stream. 3. The system of claim 1, wherein the separation unit is configured to divide the hydrocarbon feed into one light fraction stream and one heavy fraction stream. 4. The system of claim 1, wherein the light fraction stream comprises two or more light fraction streams. 5. The system of claim 1, wherein the process control unit comprises: a temperature measurement device configured to measure the temperature of the hydrocarbon feed prior to the separation unit; and wherein the one or more control units comprise a dilution control unit configured to adjust the amount of a fluid mixed with the hydrocarbon feed prior to the separation unit. 6. The system of claim 5, wherein the process control unit comprises a computer system having a set of instructions to: calculate the amount of the fluid to be mixed with the hydrocarbon feed based on the separation level and the measured temperature; andcommunicate the amount to the dilution control unit. 7. The system of claim 1, wherein the process control unit comprises: a hydrocarbon feed measurement device configured to measure flow rate of the hydrocarbon feed prior to the separation unit;a light fraction measurement device configured to measure flow rate of the at least a portion of the light fraction stream prior to the pyrolysis unit; andwherein the one or more control units comprise a light fraction control unit configured to adjust the flow rate of the at least a portion of the light fraction stream based on the separation level, the measured flow rate of the hydrocarbon feed, and the measured flow rate of the at least a portion of the light fraction stream. 8. The system of claim 7, wherein the process control unit comprises a computer system having a set of instructions to: calculate the amount of adjustment to the flow rate of the at least a portion of the light fraction stream based on the determined separation level, the measured flow rate of the hydrocarbon feed, and the measured flow rate of the at least a portion of the light fraction stream; andcommunicate the adjustment to the light fraction control unit. 9. The system of claim 1, wherein the fuel conversion unit is a boiler configured to: receive water;heat the water by burning the at least a portion of the heavy fraction stream to generate the turbine feed being steam; andpass the steam to the turbine. 10. The system of claim 1, wherein the fuel conversion unit is a partial oxidation unit and is configured to: receive an oxidant;react the oxidant and the at least a portion of the heavy fraction stream to produce the turbine feed being a gas rich in hydrogen and carbon monoxide; andpass at least a portion of the gas rich in hydrogen and carbon monoxide to the turbine. 11. The system of claim 1, wherein the pyrolysis unit comprising a convection section and a radiant section, and the separation unit is coupled between the convection section and the radiant section and is configured to provide the portion of the light fraction stream to the radiant section to create the effluent. 12. The system of claim 1, wherein the separation unit is a flash drum that divides the hydrocarbon feed into the light fraction stream and the heavy fraction stream, wherein the light fraction stream is a single light fraction stream and heavy fraction stream is a single heavy fraction stream. 13. The system of claim 1, comprising: an atmospheric distillation unit in fluid communication with the separation unit and configured to:receive a feed;separate the feed into an atmospheric bottoms stream and the hydrocarbon feed being one or more atmospheric distillate streams; andpass the hydrocarbon feed to the separation unit, wherein the separation unit comprises one or more valves in fluid communication with each other and one of the one or more valves being associated with one of one or more atmospheric distillate streams, the separation unit configured direct each one of the one or more atmospheric distillate streams into one of the heavy fraction stream or the light fraction stream. 14. The system of claim 1, comprising: an atmospheric distillation unit in fluid communication with the separation unit and configured to:receive a feed;separate the feed into an atmospheric bottoms stream and the hydrocarbon feed being one or more atmospheric distillate streams;pass the hydrocarbon feed to the separation unit,a vacuum distillation unit in fluid communication with the separation unit and the atmospheric distillation unit and configured to:receive the atmospheric bottoms stream;separate the atmospheric bottoms stream into a vacuum bottoms stream and one or more vacuum distillate streams; andpass the one or more vacuum distillate streams to the separation unit, wherein the separation unit comprises one or more valves being associated with one of one or more atmospheric distillate streams and one of one or more vacuum distillate streams, the one of one or more atmospheric distillate streams and the one of one or more vacuum distillate streams forming the hydrocarbon feed, and the separation unit configured to direct each one of the one or more atmospheric distillate streams and the one or more vacuum distillate streams into one of the heavy fraction stream or the light fraction stream.