Process for monomer recovery from a polymerization process
The present relates to a process for optimizing the recovery of unreacted monomers from a polymerization process, wherein said process comprises the steps of recovering a fluid stream generated by the separation of the polyolefin product from the polymerization fluid comprising unreacted monomers and optionally comonomers; contacting said fluid stream in an absorption zone with a scrub liquid comprising at least one C 4-10 hydrocarbons, thereby absorbing at least a portion of the unreacted monomers in said scrub liquid; and withdrawing from said absorption zone (i) a vapor overhead comprising light gas and (ii) an absorber bottoms scrub liquid comprising said C 4-10 hydrocarbons and said unreacted monomer; thereby recovering said unreacted monomer in said absorber bottoms scrub liquid comprising said C 4-10 hydrocarbons. The present invention also concerns a process for the recovery of unreacted monomers from a gas phase or slurry polymerization process, and also concerns a process for the production of polyolefins.
1. A process for recovering unreacted monomers from a gas phase polymerization process comprising:
recovering a fluid stream generated by separation of a polyolefin product from a polymerization fluid comprising unreacted monomers and optionally comonomers by purging the polymerization product with an inert gas;
contacting the fluid stream comprising the unreacted monomers, the inert gas and optionally the comonomers in an absorption zone with a scrub liquid comprising at least one C 4-10 hydrocarbon, thereby absorbing at least a portion of the unreacted monomers in the scrub liquid;
withdrawing from the absorption zone: (i) a vapor overhead comprising the inert gas, and (ii) an absorber bottoms scrub liquid comprising the C 4-10 hydrocarbon and the unreacted monomers; and
forming a flashed stream by flashing the absorber bottoms scrub liquid, and separating the flashed stream into a vapor containing the unreacted monomers and a liquid comprising the C 4-10 hydrocarbon.
2. The process of claim 1 , wherein the C 4-10 hydrocarbon is selected from hexane, hexene-1, or octane.
3. The process of claim 1 , wherein the vapor containing the unreacted monomers is compressed and recycled to the polymerization process.
4. The process of claim 1 , wherein the liquid comprising the C 4-10 hydrocarbon is cooled and pumped back to the absorption zone as the scrub liquid.
5. The process of claim 1 , wherein the fluid stream comprising the unreacted monomers, the inert gas and optionally the comonomers is compressed and cooled prior to treatment in the absorption zone.