Process and apparatus for the polymerization of ethylene

• US 7,582,723 B2
• Filed: 01/30/2006
• Issued: 09/01/2009
• Est. Priority Date: 02/04/2005
• Status: Active Grant

• Current Assignee: Basell Polyolefine GmbH (Lyondellbasell Industries NV)
• Original Assignee: Basell Polyolefine GmbH (Lyondellbasell Industries NV)
• Inventors: Ahmadzade-Youssefi, Cyrus, Nieken, Ulrich, Penzo, Giuseppe, Karer, Rainer
• Primary Examiner(s): Teskin; Fred M
• Application Number:
  US11/883,713
• Publication Number:
  US 20080177012A1
• Time in Patent Office: 1,310 Days
• Field of Search: 528/483, 528/498, 528/501, 203/71, 34/79, 526/920
• US Class Current: 528/483
• CPC Class Codes: B01J 2208/00274 involving reactant vapours
• CPC Class Codes: B01J 2208/00761 Discharging
• CPC Class Codes: B01J 2219/00006 Large-scale industrial plants
• CPC Class Codes: B01J 8/0035 Periodical feeding or evacuation
• CPC Class Codes: B01J 8/006 by filtration
• CPC Class Codes: B01J 8/24 according to "fluidised-bed" technique B01J8/20 takes precedence
• CPC Class Codes: C08F 10/00 Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
• CPC Class Codes: C08F 10/02 Ethene
• CPC Class Codes: C08F 110/02 Ethene
• CPC Class Codes: C08F 2/01 characterised by special features of the polymerisation apparatus used
• CPC Class Codes: C08F 2/34 Polymerisation in gaseous state
• CPC Class Codes: C08F 210/08 Butenes
• CPC Class Codes: C08F 210/14 Monomers containing five or more carbon atoms
• CPC Class Codes: C08F 210/16 Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
• CPC Class Codes: C08F 4/69 Chromium, molybdenum, tungsten or compounds thereof
• CPC Class Codes: C08F 6/005 from solid polymers
• CPC Class Codes: C08L 23/06 Polyethene
• CPC Class Codes: C08L 23/0815 Copolymers of ethene with aliphatic 1-olefins
• CPC Class Codes: Y02P 20/582 Recycling of unreacted starting or intermediate materials
• CPC Class Codes: Y10S 526/92 Apparatus for use in addition polymerization processes

Abstract

Process for the polymerization of ethylene or of ethylene with further 1-olefins, in which the ethylene is polymerized in the presence of a catalyst in a gas-phase reactor and reaction gas comprising propane and unpolymerized ethylene is circulated to remove the heat of polymerization, wherein the polymer particles are discharged continuously or discontinuously from the reactor, the polymer particles are separated from the major part of the concomitantly discharged gas and the polymer particles are degassed, the gas is freed of entrained fine particles and is separated from a low-boiling fraction comprising ethylene or from a high boiling fraction containing further 1-olefins or alkanes having from 4 to 12 carbon atoms in a first separation stage, a propane fraction is separated off in a second separation stage and this propane fraction is used for degassing the polymer particles discharged from the reactor, with the proportion of ethylene in the propane fraction being less than 1 mol % and the proportion of 1-olefins and alkanes having from 4 to 12 carbon atoms in the propane fraction being less than 4 mol %, in each case based on the total propane fraction. Furthermore, an apparatus for carrying out the process. In this way, a high heat discharge from the reactor, satisfactory degassing of the discharged polymer particles and recovery of the reaction gas discharged together with the polymer particles and also the gas used for degassing the polymer particles are made possible.

Claims

1. A process for the polymerizing ethylene or ethylene with further 1-olefins, in which the ethylene is polymerized in the presence of a catalyst in a gas-phase reactor to form polymer particles, the gas-phase reactor comprising a reaction gas comprising propane and unpolymerized ethylene, and the reaction gas being circulated to remove heat of polymerization;

the process comprising;

the polymer particles are discharged continuously or discontinuously from the reactor;

the polymer particles are separated from a major part of concomitantly discharged gas, and the polymer particles are degassed;

gas is freed of entrained fine particles;

in a first separation stage, gas is separated from a low-boiling fraction comprising ethylene, or from a high boiling fraction comprising further 1-olefins or alkanes, the 1-olefins or alkanes comprising from 4 to 12 carbon atoms;

in a second separation stage, a propane fraction is separated off and the propane fraction is used for degassing the polymer particles discharged from the reactor;

wherein a partial pressure of ethylene in the propane fraction used for degassing is less than 6000 Pa, and a partial pressure of a sum of further 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 10000 Pa.

2. The process according to claim 1, wherein the 1-olefins are selected from 1-butene, 1-hexene, and 1-octene, and the alkanes are selected from n-butane, n-pentane, isopentane, n-hexane and n-octane.

3. The process according to claim 1, wherein the propane fraction comprises less than 0.5 mol % of a proportion of ethylene.

4. The process according to claim 1, wherein the propane fraction comprises less than 0.2 mol % of a proportion of ethylene.

5. The process according to claim 1, wherein a partial pressure of ethylene in the propane fraction is less than 750 Pa.

6. The process according to claim 1, wherein a partial pressure of ethylene in the propane fraction is less than 300 Pa.

7. The process according to claim 1, wherein a proportion of 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 0.01 mol %.

8. The process according claim 1, wherein a proportion of 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 0.01 mol %.

9. The process according to claim 1, wherein a vapour pressure of 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 150 Pa.

10. The process according to claim 1, wherein a vapour pressure of 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 15 Pa.

11. The process according to claim 1, wherein the process further comprises circulated gas, the circulated gas comprising propane in an amount of at least 20 mol %.

12. The process according to claim 1, wherein the process further comprises circulated gas, the circulated gas comprising propane in an amount of at least 30 mol %.

13. The process according to claim 1, wherein a maximum of 10 mol % of other gases or liquids are present in addition to ethylene, further 1-olefins, hydrogen and propane in the reactor.

14. The process according to claim 1, wherein a maximum of 5 mol % of other gases or liquids are present in addition to ethylene, further 1-olefins, hydrogen and propane in the reactor.

15. The process according to claim 1, wherein the polymer particles are degassed by using the propane fraction, and the separation of the polymer particles from the major part of the discharged gas is carried out simultaneously, in the same place, or simultaneously and in the same place.

16. The process according to claim 1, wherein the reaction gas is taken from the reactor, and part of the reaction gas is condensed and is recirculated together with, or separately, from the uncondensed reactor gas.

17. The process according to claim 1, wherein the low-boiling fraction separated off in the first separation stage is recirculated to the reactor.

18. The process according to claim 1, wherein the high boiling fraction comprising further 1-olefins or alkanes comprising from 4 to 12 carbon atoms is recirculated to the reactor.

19. The process according to claim 1, wherein at least part of the ethylene separated off in the first separation stage is discharged.

20. The process according to claim 1, wherein the propane fraction is used for metered addition of at least one catalyst.

25. The process according to claim 1, wherein the reaction gas comprises propane, less than 1 mol % of ethylene, and less than 4 mol % of a proportion of 1-olefins and alkanes comprising from 4 to 12 carbon atoms.

21. An apparatus for carrying out a process for polymerizing ethylene or ethylene with further 1-olefins, in which the ethylene is polymerized in presence of a catalyst in a gas-phase reactor to form polymer particles, the gas-phase reactor comprising a reaction gas comprising propane and unpolymerized ethylene, and the reaction gas being circulated to remove heat of polymerization;

the process comprising;

the polymer particles are discharged continuously or discontinuously from the reactor;

the polymer particles are separated from a major part of concomitantly discharged gas, and the polymer particles are degassed;

gas is freed of entrained fine particles;

in a first separation stage, gas is separated from a low-boiling fraction comprising ethylene, or from a high boiling fraction comprising further 1-olefins or alkanes, the 1-olefins or alkanes comprising from 4 to 12 carbon atoms;

in a second separation stage, a propane fraction is separated off and the propane fraction is used for degassing the polymer particles discharged from the reactor;

wherein a partial pressure of ethylene in the propane fraction used for degassing is less than 6000 Pa, and a partial pressure of a sum of further 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 10000 Pa;

the apparatus comprising;

a gas-phase reactor comprising a bed of polymer particles;

a recycle gas line connected to the reactor for carrying away and recirculating reaction gas, wherein the reaction gas comprises propane and unpolymerized ethylene;

a product offtake line for continuously or discontinuously taking off polymer particles from the reactor, wherein the product offtake line is connected to a degassing vessel for separating polymer particles and gas;

a particle precipitation unit connected to the degassing vessel for freeing gas of entrained fine particles;

a first separation unit connected to the particle precipitation unit for separating off a low-boiling fraction comprising ethylene and ethane;

a second separation unit connected to a bottom of the first separation unit for separating off a propane fraction;

a propane line which is connected to a top of the second separation unit and in turn is connected to the degassing vessel to degas the polymer particles using the propane fraction;

wherein the first separation unit is such that the partial pressure of ethylene in the propane fraction entering the degassing vessel is less than 6000 Pa, and the second separation unit is such that the partial pressure of 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction entering the degassing vessel is less than 10000 Pa.

23. The apparatus according to claim 21, wherein the first separation unit, the second separation unit, or a combination thereof carry out a separation by distillation.

22. An apparatus for carrying out a process for polymerizing ethylene or ethylene with further 1-olefins, in which the ethylene is polymerized in presence of a catalyst in a gas-phase reactor to form polymer particles, the gas-phase reactor comprising a reaction gas comprising propane and unpolymerized ethylene, and the reaction gas being circulated to remove heat of polymerization;

the process comprising;

the polymer particles are discharged continuously or discontinuously from the reactor;

the polymer particles are separated from a major part of concomitantly discharged gas, and the polymer particles are degassed;

gas is freed of entrained fine particles;

in a first separation stage, gas is separated from a low-boiling fraction comprising ethylene, or from a high boiling fraction comprising further 1-olefins or alkanes, the 1-olefins or alkanes comprising from 4 to 12 carbon atoms;

in a second separation stage, a propane fraction is separated off and the propane fraction is used for degassing the polymer particles discharged from the reactor;

wherein a partial pressure of ethylene in the propane fraction used for degassing is less than 6000 Pa, and a partial pressure of a sum of further 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction is less than 10000 Pa;

the apparatus comprising;

a gas-phase reactor comprising a bed of polymer particles;

a recycle gas line connected to the reactor for carrying away and recirculating reaction gas, wherein the reaction gas comprises propane and unpolymerized ethylene;

a product offtake line for continuously or discontinuously taking off polymer particles from the reactor, wherein the product offtake line is connected to a degassing vessel for separating polymer particles and gas;

a particle precipitation unit connected to the degassing vessel for freeing gas of entrained fine particles;

a first separation unit connected to a particle precipitation unit for separating off a high-boiling fraction comprising further 1-olefins, alkanes comprising 4 to 10 carbon atoms, or mixtures thereof;

a second separation unit connected to a top of the first separation unit for separating off a propane fraction;

a propane line connected to a bottom of the second separation unit and in turn is connected to the degassing vessel to degas the polymer particles using the propane fraction after passing an evaporation unit;

wherein the first separation unit is such that the partial pressure of ethylene in the propane fraction entering the degassing vessel is less than 6000 Pa, and the second separation unit is such that the partial pressure of 1-olefins and alkanes comprising from 4 to 12 carbon atoms in the propane fraction entering the degassing vessel is less than 10000 Pa.

24. The apparatus according to claim 22, wherein the first separation unit, the second separation unit, or a combination thereof carry out a separation by distillation.