Process for preparing fatty acid ester sulfonate
A technology for ester sulfonate and fatty acid, which is applied in the field of preparing fatty acid ester sulfonate, can solve the problems of thickening of liquid film, easy explosion and high viscosity, and achieves strong low temperature washing ability, good hard water resistance and low temperature water solubility. good effect
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Embodiment 1
[0026] Example 1: n-hexanoic acid enters SO at 20°C 3 Gas jet sulfonation reactor, SO 3 / air (volume ratio 10%) mixed gas enters SO at 60°C 3 Gas injection sulfonation reactor, the gas velocity from the gas nozzle is 100m / s, n-hexanoic acid / SO 3 The feed molar ratio is 1:1.0, the reaction time of the two in the reactor body is 5 seconds, the sulfonated product and unreacted SO 3 / air mixture from SO 3 After the product outlet of the gas jet sulfonation reactor is discharged, the gas-liquid separation is carried out. After the liquid phase is cooled, the reaction is continued at 50°C for 60 minutes to obtain α-sulfocaproic acid, and the gas phase is SO 3 / air mixed gas, the mixed gas can be recycled.
[0027] Add α-sulfocaproic acid and cetyl alcohol in the esterification reactor, the mol ratio of the two is 1: 1.1, with the total mass of α-sulfo fatty acid and cetyl alcohol, add 300% heptane (boiling point 98.4°C), and reacted under reflux for 0.5h to obtain cetyl hexanoa...
Embodiment 2
[0029] C 1214 Mixed fatty acids enter SO at 40°C 3 Gas jet sulfonation reactor, SO 3 / air (volume ratio 15%) mixed gas enters SO at 65°C 3Gas injection sulfonation reactor, the gas velocity from the gas nozzle is 125m / s, C 1214 Mixed Fatty Acids / SO 3 The feed molar ratio is 1:1.2, the reaction time of the two in the reactor body is 6 seconds, the sulfonated product and unreacted SO 3 / air mixture from SO 3 After the product outlet of the gas jet sulfonation reactor is discharged, the gas-liquid separation is carried out. After the liquid phase is cooled, the reaction is continued at 180°C for 10 minutes to obtain α-sulfo C 1214 acid.
[0030] Add α-sulfo C in the esterification reaction kettle 1214 Acid and n-decyl alcohol, the molar ratio of the two is 1:1.2, with α-sulfo C 1214 Based on the total mass of acid and n-decyl alcohol, 200% n-hexane (boiling point 68.7° C.) was added in different proportions, and reacted for 2 h under reflux to obtain C 1214 Decyl sulfoni...
Embodiment 3
[0032] Hexadecanoic acid enters SO at 100°C 3 Gas jet sulfonation reactor, SO 3 / air (20% by volume) mixed gas enters SO at 80°C 3 Gas injection sulfonation reactor, the gas velocity from the gas nozzle is 225m / s, n-hexadecanic acid / SO 3 The feed molar ratio is 1:2.0, the reaction time of the two in the reactor body is 10 seconds, the sulfonated product and unreacted SO 3 / air mixture from SO 3 After the product outlet of the gas jet sulfonation reactor is discharged, the gas-liquid separation is carried out. After the liquid phase is cooled, the reaction is continued at 160° C. for 120 minutes to obtain α-sulfohexadecanoic acid.
[0033] Add α-sulfocetanoic acid and 2-ethylhexanol into the esterification reaction kettle, the molar ratio of the two is 1:1.1, without solvent, react at 30°C for 24h to obtain α-sulfocetanoic acid 2-Ethylhexanol ester. Add 80% ethanol / water solution by volume to the neutralization tank, add potassium hydroxide to prepare potassium hydroxide e...
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