Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US2024131490A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024131490-A1 |
| Application number | US-202318509702-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 15, 2023 |
| Priority date | Aug 12, 2016 |
| Publication date | Apr 25, 2024 |
| Grant date | — |
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The invention generally relates to systems and methods for increasing reaction yield. In certain embodiments, the invention provides systems for increasing a yield of a chemical reaction that include a pneumatic sprayer configured to generate a liquid spray discharge from a solvent. The solvent includes a plurality of molecules, a portion of which react with each other within the liquid spray discharge to form a reaction product. The system also includes a collector positioned to receive the liquid spray discharge including the unreacted molecules and the reaction product. The system also includes a recirculation loop connected from the collector to the pneumatic sprayer in order to allow the unreacted molecules and the reaction product to be recycled through the pneumatic sprayer, thereby allowing a plurality of the unreacted molecules to react with each other as the unreacted molecules cycle again through the system.
Opening claim text (preview).
1 - 20 . (canceled) 21 . A method for increasing yield of a chemical reaction, the method comprising: generating a liquid spray discharge using a pneumatic sprayer, wherein the liquid spray discharge is generated from a solvent that comprises a plurality of molecules, a portion of which react with each other within the liquid spray discharge to form a reaction product, wherein the reaction is monitored in real-time; collecting in a collector the liquid spray discharge comprising unreacted molecules and the reaction product; and recirculating the unreacted molecules and the reaction product through the pneumatic sprayer, in order to allow a plurality of the unreacted molecules in the solvent to react with each other as the unreacted molecules cycle again through the pneumatic sprayer, thereby increasing a yield of the chemical reaction. 22 . The method according to claim 21 , wherein a voltage source is operably associated with the pneumatic sprayer in order to generate a charged liquid spray discharge. 23 . The method according to claim 22 , wherein collecting comprises condensing the liquid spray discharge into a reservoir of the collector. 24 . The method according to claim 23 , wherein condensing uses a cryogenic condenser. 25 . The method according to claim 23 , wherein collecting further comprises precipitating liquid droplets from any liquid spray discharge not captured in the condensing step. 26 . The method according to claim 25 , further comprising degassing gas used by the pneumatic sprayer to generate the liquid spray discharge. 27 . The method according to claim 25 , wherein degassing uses a liquid degassing unit comprising a semi-permeable membrane within a vacuum chamber. 28 . The method according to claim 26 , further comprising analyzing the reaction product. 29 . The method according to claim 21 , wherein the pneumatic sprayer is an electrosonic spray ionization source. 30 . The method according to claim 21 , further comprising controlling an extent of formation of the reaction product by varying a distance between the pneumatic sprayer and the collector.
externally, i.e. the mixture leaving the vessel and subsequently re-entering it · CPC title
with degasification or deaeration · CPC title
by filtration · CPC title
Nozzle-type elements (nozzle-type reactors B01J19/26) · CPC title
Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor (B01J8/00, B01J19/08 take precedence) · CPC title
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