Sulfur trioxide gas jet sulfonation process and device for bisalkyl benzene
A technology of heavy alkylbenzene and gas injection, which is applied in chemical/physical/physicochemical nozzle reactors, sulfonic acid preparation, organic chemistry, etc. It can solve problems such as difficult sulfonation, long residence time, and increased production costs. Achieve the effects of convenient operation and maintenance, stable product quality, and low equipment investment
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Embodiment 1
[0026] Example 1: Sulfonation of heavy alkylbenzenes
[0027] SO 3 The gas jet sulfonation reactor is composed of a nozzle and a reactor body. The nozzle is composed of a gas nozzle 3, a liquid distribution chamber 4, an atomizing nozzle 5, a heavy alkylbenzene inlet 1 and a mixed gas inlet 2, and the gas nozzle 3 Connected with the mixed gas inlet 2 and fixed on the top of the liquid distribution chamber 4, the heavy alkylbenzene inlet 1 is located at the lower part of the side of the liquid distributor 4, the atomizing nozzle 5 is fixed in the liquid distribution chamber 4, and the lower part of the gas nozzle 3 enters the atomizing nozzle 5, the top of the atomizing nozzle 5 is open, the position of the top of the atomizing nozzle 5 in the liquid distribution chamber 4 is higher than the position of the heavy alkylbenzene inlet 1 in the liquid distribution chamber 4, and the nozzle is fixed on the reactor body 7 The top and the lower part of the atomizing nozzle 5 enter th...
Embodiment 2
[0029] Example 2: Sulfonation of heavy alkylbenzenes
[0030] Heavy alkylbenzene (average molar mass: 345) was continuously converted from SO at a flow rate of 10kg / h at 45°C 3 The liquid phase inlet 1 of the gas jet sulfonation reactor enters the liquid distribution chamber 4, then overflows into the atomizing nozzle 5 through the top overflow of the atomizing nozzle 5, and then flows downward along the inner wall of the atomizing nozzle 5, SO 3 / air (volume ratio 6%) mixed gas by SO at 65°C 3 The gas phase inlet 2 of the gas injection sulfonation reactor enters the gas nozzle 3 and the gas velocity ejected from the gas nozzle 3 is 238m / s, SO 3 / heavy alkylbenzene feed molar ratio 1.2:1, SO 3 / Air mixed gas contacts with heavy alkyl benzene and is sprayed into reactor still body (7) from atomizing nozzle to react together, and the reaction time in reactor still body (7) is 3 seconds, and the sulfonated reaction product obtained and unreacted SO 3 / air mixture from SO 3 A...
Embodiment 3
[0031] Example 3: Sulfonation of heavy alkylbenzenes
[0032] Heavy alkylbenzene (average molar mass: 320) was continuously converted from SO at a flow rate of 9.5kg / h at 40°C 3 The liquid phase inlet 1 of the gas jet sulfonation reactor enters the liquid distribution chamber 4, then overflows into the atomizing nozzle 5 through the top overflow of the atomizing nozzle 5, and then flows downward along the inner wall of the atomizing nozzle 5, SO 3 / air (volume ratio 4%) mixed gas by SO at 60°C 3 The gas phase inlet 2 of the gas injection sulfonation reactor enters the gas nozzle 3 and the gas velocity ejected from the gas nozzle 3 is 193m / s, SO 3 / heavy alkylbenzene feed molar ratio 1.15:1, SO 3 / Air mixed gas contacts with heavy alkyl benzene and is sprayed into reactor still body (7) from atomizing nozzle to react together, and the reaction time in reactor still body (7) is 4 seconds, and the sulfonated reaction product obtained and unreacted SO 3 / air mixture from SO 3...
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