Solution polymerization process with improved energy utilization
US-2016229930-A1 · Aug 11, 2016 · US
US10047178B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10047178-B2 |
| Application number | US-201715426670-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 7, 2017 |
| Priority date | Feb 7, 2017 |
| Publication date | Aug 14, 2018 |
| Grant date | Aug 14, 2018 |
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This disclosure relates to a process for polymerization, and in particular to minimizing undesired polymerization reactions downstream of a polymerization reaction zone, for instance by use of a quenching agent that enables fast reaction rates with active polymerization catalyst in the polymerization effluent, so as to quench the catalyst quickly, thereby preventing uncontrolled polymerization reactions. A preferred quenching agent is methanol. Also provided are means for treating polymer recycle streams containing oxygenates, which may result from the use of such quench agents, particularly in polymerization processes including polyene (e.g., diene) monomers.
Opening claim text (preview).
The invention claimed is: 1. A process comprising: (a) feeding one or more monomers and a polymerization solvent to a solution polymerization reaction zone; (b) polymerizing at least a portion of the one or more monomers in the presence of a polymerization catalyst in the solution polymerization reaction zone; (c) withdrawing a polymerization effluent from the polymerization reaction zone, wherein the polymerization effluent comprises active polymerization catalyst and one or more unreacted monomers; (d) adding a quenching agent which consists of methanol and water to the polymerization effluent so as to quench the active polymerization catalyst in the polymerization effluent, thereby forming a quenched polymer stream; and (e) recovering solid polymer product from the quenched polymer stream, wherein the quenching agent quenches the active polymerization catalyst at a quenching rate such that the solid polymer product, when extruded as a cast film, has a mean gel count of 10 m −2 or less. 2. The process of claim 1 , wherein recovering solid polymer product comprises: (I) separating the quenched polymer stream into a polymer product stream and a polymer recycle stream; and (II) devolatilizing the polymer product stream so as to recover the solid polymer product. 3. The process of claim 2 , further comprising: (I-a) contacting at least a portion of the polymer recycle stream with an adsorbent bed comprising at least two adsorbents so as to produce a treated recycle stream. 4. The process of claim 1 , wherein the one or more monomers comprise one or more polyenes. 5. The process of claim 4 , wherein the one or more monomers comprise ethylene, propylene, and a diene. 6. The process of claim 4 , wherein the quenched polymer stream comprises C 10 and C 19 oxygenates. 7. The process of claim 3 , wherein the adsorbent bed comprises a zeolitic molecular sieve and a hybrid zeolite in alumina. 8. The process of claim 7 , wherein the adsorbent bed further comprises at least one silica adsorbent. 9. The process of claim 7 , wherein the zeolitic molecular sieve comprises material selected from the group consisting of zeolite X, zeolite Y, zeolite A, faujasite, mordenite, ferrierite, and mixtures thereof. 10. The process of claim 1 , wherein the quenching rate is such that the solid polymer product has a mean gel count of 9 m −2 or less.
with non-conjugated dienes, e.g. EPT rubbers · CPC title
Use as polymer for film forming · CPC title
Propene · CPC title
using short-stopping agents · CPC title
Removal of residual monomers by physical means · CPC title
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