# US 10,246,473 B2 · Process for preparing an acryloyloxysilane > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,246,473 B2 - Document ID: US10246473B2 - Status: Granted - Kind: B2 - Application number: 15/567,391 - Filed: 2016-06-17 - Published: 2018-05-17 - Granted: 2019-04-02 - Earliest claimed: 2015-06-19 - Assignees: Dow Corning Corporation - Applicants: Dow Corning Corporation - Inventors: Michael A. Depierro; Sean P Reisch - Web page: https://patentgrep.com/patent/US10246473B2 ## CPC - C07F 7/20: Purification, separation - C07F 7/1804: {Compounds having Si-O-C linkages (Si-O-acyl linkages C07F7/1896)} - C07F: ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM (metal-containing porphyrins C07D487/22) ## Abstract A process for purifying an acryloyloxysilane comprising subjecting a mixture comprising an acryloyloxysilane, a haloorganoalkoxysilane, and an alkane-based non-polar solvent to a temperature and pressure sufficient to vaporize a portion of the non-polar solvent, the haloorganoalkoxysilane, or the non-polar solvent and the haloorganoalkoxysilane from the mixture to produce a purified mixture comprising the acryloyloxysilane. The examples disclose a three-step short-path distillation process, where in the first two passes, the residue-fraction is the one containing the product, whereas in the third path, the distillate is containing the purified product. ## Claims ### Claim 1 A process for purifying an acryloyloxysilane, the process comprising: subjecting a mixture comprising an acryloyloxysilane, a haloorganoalkoxysilane, and a non-polar solvent, wherein the non-polar solvent comprises a mixture of 0.5 to 15% (w/w) of a branched-chain alkane having from 5 to 20 carbon atoms and 85 to 99.5% (w/w) of a straight-chain alkane having from 5 to 14 carbon atoms, based on the weight of the branched-chain and straight-chain alkane in the non-polar solvent, and wherein the non-polar solvent comprises less than 5% (w/w), based on the weight of the non-polar solvent, of an aromatic compound, to a temperature and pressure sufficient to vaporize a portion of the non-polar solvent, the haloorganoalkoxysilane, or the non-polar solvent and the haloorganoalkoxysilane from the mixture to produce a purified mixture comprising the acryloyloxysilane. ### Claim 2 (depends on 1) The process according to claim 1, wherein the process is repeated one or more times using the purified mixture as the mixture comprising an acryloyloxysilane, a haloorganoalkoxysilane, and a non-polar solvent. ### Claim 3 (depends on 2) The process of claim 2, wherein the purified mixture is conveyed from the outlet of the thin film evaporator, wiped film evaporator, falling film evaporator, or short path distillation unit to the inlet of the same or different thin film evaporator, wiped film evaporator, falling film evaporator, or short path distillation unit to perform the heating of the purified mixture and repeat the process. ### Claim 4 (depends on 3) The process of claim 3, wherein the mixture or the purified mixture are flow through the thin film evaporator, the wiped film evaporator, the falling film evaporator, the short path distillation unit at a flow rate of from 10 to 100 kg/hr·m2. ### Claim 5 (depends on 2) The process of claim 2, wherein the temperature and pressure vary from one process repetition to another. ### Claim 6 (depends on 2) The process of claim 2, wherein the process is conducted using a thin film evaporator, a wiped film evaporator, a falling film evaporator, a short path distillation unit, or a series of thin film evaporators, wiped film evaporators, falling film evaporators, short path distillation units. ### Claim 7 (depends on 1) The process according to claim 1, further comprising subjecting the purified mixture to a temperature and pressure sufficient to vaporize the acryloyloxysilane, condensing the vaporized acryloyloxysilane, and collecting the condensed acryloyloxysilane to form a final purified acryloyloxysilane product. ### Claim 8 (depends on 7) The process of claim 7, wherein the process is conducted using a thin film evaporator, a wiped film evaporator, a falling film evaporator, a short path distillation unit, or a series of thin film evaporators, wiped film evaporators, falling film evaporators, short path distillation units. ### Claim 9 (depends on 8) The process of claim 8, wherein the mixture or the purified mixture are flow through the thin film evaporator, the wiped film evaporator, the falling film evaporator, the short path distillation unit at a flow rate of from 10 to 100 kg/hr·m2. ### Claim 10 (depends on 7) The process of claim 7, wherein the temperature and pressure vary from one process repetition to another. ### Claim 11 (depends on 1) The process of claim 1, where the temperature is from 50° C. to 230° C. and the pressure is from 0 to 102 kPa. ### Claim 12 (depends on 1) The process of claim 1, wherein the the acryloyloxysilane has the formula CR62=CR1COOR3Si(OR4)nR53−n (IV), wherein R1 is H, R7COO−Ma+, or C1-C6 hydrocarbyl, R3 is C1-C6 hydrocarbylene, each R4 is independently C1-C10 hydrocarbyl, each R5 is independently R1, each R6 is independently H, C1-C6 hydrocarbyl, or COOR3Si(OR4)nR53−n, R7 is hydrocarbylene having from 1 to 6 carbon atoms, n is an integer from 1 to 3, Ma+is an alkali metal cation or alkaline earth metal cation, a is the cationic charge and has a value of 1 or 2. ### Claim 13 (depends on 12) The process of claim 12, wherein the acryloyloxysilane is γ-acryloyloxypropylmethyldimethoxysilane, γ-acryloyloxypropyltrimethoxysilane, γ-sorbyloxypropylmethyldimethoxysilane, γ-sorbyloxypropyltrimethoxysilane, γ-acryloyloxypropyltriethoxysilane, γ-sorbyloxypropyltriethoxysilane, bis(γ-trimethoxysilylpropyl) fumarate, or bis(γ-triethoxysilylpropyl) fumarate. ### Claim 14 (depends on 1) The process of claim 1, comprising forming the mixture comprising the acryloyloxysilane, the haloorganoalkoxysilane, and the non-polar solvent by i) combining the branched-chain alkane having from 5 to 20 carbon atoms during a reaction to form the acryloyloxysilane, ii) combining the branched-chain alkane having from 5 to 20 carbon atoms with the acryloyloxysilane and the haloorganoalkoxysilane after the reaction to form the acryloyloxysilane, or iii) combining the branched-chain alkane having from 5 to 20 carbon atoms with the acryloyloxysilane and the haloorganoalkoxysilane after the reaction to form the acryloyloxysilane and after subjecting the acryloyloxysilane formed by the reaction to an initial purification process. ### Claim 15 (depends on 1) The process of claim 1, wherein the straight-chain alkane is n-heptane and non-polar solvent comprises a mixture of branched-chain alkanes having from 8 to 14 carbon atoms. ### Claim 16 (depends on 1) The process of claim 1, where the non-polar solvent has a boiling point lower than boiling point of the acryloyloxysilane. ### Claim 17 (depends on 1) The process of claim 1, where the non-polar solvent further comprises an additional component selected from the group consisting of cyclopentane, cyclohexane, cyclooctane, cyclohexane, cis-cyclooctene, tert-butyl methyl ether and di-n-butyl ether. ### Claim 18 (depends on 1) The process of claim 1, wherein the process is conducted using a thin film evaporator, a wiped film evaporator, a falling film evaporator, a short path distillation unit, or a series of thin film evaporators, wiped film evaporators, falling film evaporators, short path distillation units. ### Claim 19 (depends on 1) The process according to claim 1, further comprising subjecting the purified mixture to a temperature and pressure sufficient to vaporize the acryloyloxysilane, condensing the vaporized acryloyloxysilane, and collecting the condensed acryloyloxysilane to form a final purified acryloyloxysilane product.