초록 ▼

Methods for controlling the temperature of an olefin polymerization reactor (e.g., a polyethylene reactor) system are disclosed herein. The olefin polymerization reactor system includes a polymerization reactor and a cooling jacket in thermal contact with the reactor. An aqueous froth is present in

Methods for controlling the temperature of an olefin polymerization reactor (e.g., a polyethylene reactor) system are disclosed herein. The olefin polymerization reactor system includes a polymerization reactor and a cooling jacket in thermal contact with the reactor. An aqueous froth is present in the jacket, and the pressure therein is maintained below atmospheric pressure. Control of the pressure in the jacket controls the boiling temperature of the jacket fluid, and thus, controls the rate of heat transfer from the reactor to the fluid in the jacket. This provides an efficient and simple means for controlling the reactor temperature.

대표청구항 ▼

1. A method for controlling the temperature of an olefin polymerization reactor system that includes a polymerization reactor and a cooling jacket in thermal contact with the reactor, comprising:(a) supplying an aqueous froth to the cooling jacket, wherein the pressure in the jacket is lower than at

1. A method for controlling the temperature of an olefin polymerization reactor system that includes a polymerization reactor and a cooling jacket in thermal contact with the reactor, comprising:(a) supplying an aqueous froth to the cooling jacket, wherein the pressure in the jacket is lower than atmospheric pressure, and wherein heat transferred from the reactor to the jacket causes at least some of the water in the aqueous froth to vaporize, thereby forming a vapor phase and a first liquid phase,(b) separating the vapor phase and the first liquid phase at a pressure that is lower than atmospheric pressure, and(c) condensing at least a fraction of the vapor phase to form a second liquid phase at a pressure that is lower than atmospheric pressure. 2. The method of claim 1, further comprising:combining the second liquid phase and the first liquid phase, thereby producing a collected recycle water stream, and recycling the collected recycle water stream to the jacket. 3. The method of claim 2, wherein the collected recycle water stream is superheated to between 10 and 15 degrees Fahrenheit over the temperature at which the collected recycle water stream boils when at cooling jacket pressure. 4. The method of claim 1, wherein a vacuum pump is used to maintain a pressure less than atmospheric pressure in steps (a), (b), and (c). 5. The method of claim 2, wherein the pressure in the jacket is adjusted so as to maintain a desired temperature in the reactor. 6. The method of claim 1, wherein ethylene is polymerized in the reactor to produce polyethylene. 7. The method of claim 1, wherein ethylene and at least one other alpha-olefin are co-polymerized in the reactor. 8. The method of claim 7, wherein the at least one other alpha-olefin comprises from four to twelve carbon atoms. 9. The method of claim 1, wherein the reactor is a loop reactor. 10. The method of claim 1, wherein the aqueous froth that is supplied to the jacket comprises between about 95% to 99% by weight liquid. 11. The method of claim 10, wherein the aqueous froth that is supplied to the jacket comprises between about 97% to 99% by weight liquid. 12. The method of claim 1, wherein the aqueous froth is supplied to the cooling jacket as a downflow. 13. The method of claim 1, wherein the aqueous froth is supplied to the cooling jacket as an upflow. 14. A method for controlling the temperature of an olefin polymerization reactor system that includes a polymerization reactor and a cooling jacket in thermal contact with the reactor, comprising:(i) supplying a downflow aqueous solution to the cooling jacket, wherein the pressure in the jacket is lower than atmospheric pressure, and wherein heat transferred from the reactor to the jacket causes at least some of the water in the aqueous solution to vaporize, thereby forming a vapor phase and a first liquid phase,(ii) separating the vapor phase and the first liquid phase at a pressure that is lower than atmospheric pressure, and(iii) condensing at least a fraction of the vapor phase to form a second liquid phase at a pressure that is lower than atmospheric pressure. 15. The method of claim 14, further comprising:combining the second liquid phase and the first liquid phase, thereby producing a collected recycle water stream, and recycling the collected recycle water stream to the jacket. 16. The method of claim 15, wherein the collected recycle water stream is superheated to between 10 and 15 degrees Fahrenheit over the temperature at which the collected recycle water stream boils when at cooling jacket pressure. 17. The method of claim 14, wherein a vacuum pump is used to maintain a pressure less than atmospheric pressure in steps (a), (b), and (c). 18. The method of claim 15, wherein the pressure in the jacket is adjusted so as to maintain a desired temperature in the reactor. 19. The method of claim 14, wherein ethylene is polymerized in the reactor to produce polyethylene. 20. The method of claim 14, wherein ethylene and at least one other alpha-olefin are co-polymerized in the reactor. 21. The method of claim 20, wherein the at least one other alpha-olefin comprises from four to twelve carbon atoms. 22. The method of claim 14, wherein the reactor is a loop reactor. 23. A method for controlling the temperature of an olefin polymerization reactor system that includes a polymerization reactor, and a cooling jacket in thermal contact with the reactor, wherein at least one alpha-olefin having from two to twelve carbon atoms is polymerized in the reactor, comprising:(A) supplying an aqueous froth to the cooling jacket, wherein the pressure in the jacket is lower than atmospheric pressure, and wherein heat transferred from the reactor to the jacket causes at least some of the water in the aqueous froth to vaporize, thereby forming a vapor phase and a first liquid phase,(B) separating the vapor phase and the first liquid phase at a pressure that is lower than atmospheric pressure,(C) condensing at least a fraction of the vapor phase to form a second liquid phase at a pressure that is lower than atmospheric pressure,wherein a vacuum pump is used to maintain a pressure less than atmospheric pressure in steps (A), (B), and (C), and the pressure in the jacket is adjusted so as to maintain a desired temperature in the reactor,(D) combining the second liquid phase and the first liquid phase, thereby producing a collected recycle water stream,(E) superheating the collected recycle water stream to between 10 and 15 degrees Fahrenheit over the temperature at which the collected recycle water stream boils when at cooling jacket pressure, and(F) recycling the collected recycle water stream to the jacket.