Process for preparing methylmercaptopropionaldehyde
View Patent ↗A process for preparing methylmercaptopropionaldehyde in a single reaction unit, is provided. According to the preferred embodiment, the process comprises, simultaneously contacting a gaseous mixture comprising acrolein with a liquid mixture comprising methylmercaptopropionaldehyde, methyl mercaptan, a catalyst and methylmercaptopropionaldehyde methyl thiohemiacetal in the reactive absorber; absorbing the acrolein from the gaseous mixture into the liquid mixture; reacting the absorbed acrolein with the methyl mercaptan or the methylmercaptopropionaldehyde methyl thiohemiacetal to obtain methylmercapto-propionaldehyde; removing gaseous impurities and by-products from the liquid mixture; and separating the obtained methylmercaptopropionaldehyde product from the reactive absorber, directing a portion of the separated product to storage or further processing and recycling the remaining portion to the reactive absorber; wherein the methyl mercaptan optionally comprises dimethyl sulfide or dimethyl ether.
1. A process for preparing methylmercaptopropionaldehyde in a single reaction unit, comprising, simultaneously:
contacting a gaseous mixture comprising acrolein with a liquid mixture comprising methylmercaptopropionaldehyde, methyl mercaptan, a catalyst and methylmercaptopropionaldehyde methyl thiohemiacetal in the reaction unit;
absorbing the acrolein from the gaseous mixture into the liquid mixture;
reacting the absorbed acrolein with the methyl mercaptan or the methylmercaptopropionaldehyde methyl thiohemiacetal to obtain methylmercaptopropionaldehyde;
removing gaseous impurities and by-products from the liquid mixture; and
separating the obtained methylmercaptopropionaldehyde product from the reaction unit, directing a portion of the separated product to storage or further processing and recycling the remaining portion to the reaction unit;
wherein the methyl mercaptan optionally comprises dimethyl sulfide or dimethyl ether; and
wherein a concentration of the methylmercaptopropionaldehyde methyl thiohemiacetal in the liquid mixture is from 1 to 10% by weight.
2. The process according to claim 1 , wherein the gaseous impurities and by-products are removed from the reactive absorber by stripping at a temperature of 5 to 70 ° C. and pressure of 0.3 to 5 bar.
3. The process according to claim 1 , wherein the gaseous impurities and by-products comprise at least one compound selected from the group consisting of dimethyl sulfide, acetaldehyde, water, dimethyl disulphide, methanol, carbon dioxide, propane, propene, hydrogen sulfide and dimethyl ether.
4. The process according to claim 1 , wherein the methyl mercaptan is supplied to the reaction unit continuously as a liquid, a gas or a mixture of liquid and gas.
5. The process according to claim 1 , wherein the catalyst is a homogeneous catalyst, a heterogeneous catalyst or a combination thereof.
6. The process according to claim 1 , wherein the catalyst is at least one of dimethylbenzylamine and triethanolamine.
7. The process according to claim 1 , wherein a concentration of the catalyst in the liquid mixture is from 50 to 500 ppmw.
8. The process according to claim 1 , further comprising:
adjusting a mol ratio of methyl mercaptan to acrolein in the liquid mixture to a value between 0.95 and 1.1 mol/mol.
9. The process according to claim 8 , the adjustment of the ratio of methyl mercaptan to acrolein in the liquid mixture comprises an inline determination of the ratio via near infrared (NIR) measurement.
10. The process according to claim 1 , further comprising:
adjusting a feed rate of the gaseous acrolein to the reaction unit by a method comprising determination of an acrolein concentration in the gaseous mixture with inline Fourier transform infrared (FTIR) measurement.
11. The process according to claim 1 , further comprising continuously adding at least one compound from the group consisting of inorganic and organic acids to the liquid mixture.
12. The process according to claim 1 , wherein the methyl mercaptan comprises 1.5-5% by weight of dimethyl sulphide and 0-3% by weight of dimethyl ether.
13. The process according to claim 1 , wherein a water content of the product methylmercaptopropionaldehyde is less than 2.5% by weight.
14. The process according to claim 8 , wherein a mol ratio of methyl mercaptan to acrolein in the liquid mixture is between 1.004 and 1.009 mol/mol.
15. The process according to claim 1 , wherein a residue concentration of the methylmercaptopropionaldehyde is 0.25% by weight or less.
16. The process according to claim 11 wherein an inorganic acid is added to the reaction unit and the inorganic acid is at least one selected from the group consisting of sulfuric acid, phosphoric acid, hydrogen fluoride, hydrogen chloride and hydrogen bromide.
17. The process according to claim 11 wherein an organic acid is added to the reaction unit and the organic acid is at least one selected from the group consisting of acetic acid, formic acid, propionic acid, octanoic acid, acrylic acid, tartaric acid, trichloroacetic acid, trifluoroacetic acid, oxalic acid, succinic acid, adipic acid, phenylacetic acid, benzoic acid, cinnamic acid, furoic acid, thiophenecarboxylic acid and phthalic acid.
18. The process according to claim 1 , further comprising continuously adding at least one compound from the group consisting of inorganic and organic bases to the liquid mixture.
19. The process according to claim 18 , wherein an organic base is added to the reaction unit and the organic base is selected from the group consisting of triethanolamine, piperidine, triethylamine, pyridine, quinoline, urotropin and N, N-dimethylaniline.
20. The process according to claim 1 , wherein the single reaction unit is a reactive a reactive absorber.