Device for producing chlorosulfonic acid by m/p-phthaloyl chloride induced air and process thereof
A technology for phthaloyl chloride induced air and production equipment, which is applied in the field of iso/terephthaloyl chloride induced air to produce chlorosulfonic acid, and can solve the problems of high impurity content in by-products, waste of resources, and large consumption of water and liquid caustic soda and other issues, to achieve the effect of increasing the added value of products, reducing waste gas emissions, and realizing recycling
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Embodiment 1
[0049] The device for producing chlorosulfonic acid by introducing air from terephthaloyl dichloride described in present embodiment 1 includes air pretreatment device, chlorosulfonic acid production unit and sulfur dioxide treatment recovery device; Device 5 is divided into two roads by pipeline, is respectively connected with the bottom side of primary reaction tower 6 and secondary reaction tower 7 in the chlorosulfonic acid production plant, and the top of secondary reaction tower 7 in the chlorosulfonic acid production plant passes through The pipeline is connected with the sulfur distribution reactor 17 in the sulfur dioxide treatment and recovery device.
[0050] The induced air pretreatment device includes an absorption tower 3, an induced air condenser 4 and a mist catcher 5, the upper side of the absorption tower 3 is connected to the thionyl chloride feed line 1, and the lower side of the absorption tower 3 is connected to the m / t The formyl chloride induced air fee...
Embodiment 2
[0074] Embodiment 2 is identical with the device and technology thereof that the inter / terephthaloyl dichloride described in embodiment 1 induces air to produce chlorosulfonic acid, and difference is:
[0075] Inter / terephthaloyl dichloride leads to air, in mass percentage, the raw material composition is as follows: HCl 10%, SO 2 22%, acid chloride 3% and air 63%.
[0076] The absorbent is thionyl chloride, and the outlet temperature of induced draft condenser 4 is 32°C.
[0077] Both the primary reaction tower 6 and the secondary reaction tower 7 are provided with cooling jackets for circulating water.
[0078] The gas phase residence time in the sulfur matching reactor 17 is 7s.
[0079] The primary reaction tower 6 controls the temperature at 80-90°C.
[0080] The outlet temperature of the primary circulating condenser 9 is controlled to be 45°C.
[0081] The outlet temperature of the primary product condenser 11 is controlled to be 38°C.
[0082] The temperature of ...
Embodiment 3
[0087] Embodiment 3 is identical with the device and technology thereof that the inter / terephthaloyl dichloride described in embodiment 1 induces air to produce chlorosulfonic acid, and difference is:
[0088] Inter / terephthaloyl dichloride leads to air, in mass percentage, the raw material composition is as follows: HCl 10%, SO 2 22%, acid chloride 3% and air 63%.
[0089] The absorbent is thionyl chloride, and the outlet temperature of induced draft condenser 4 is 30°C.
[0090] Both the primary reaction tower 6 and the secondary reaction tower 7 are provided with cooling jackets for circulating water.
[0091] The gas phase residence time in the sulfur matching reactor 17 is 10s.
[0092] The temperature of primary reaction tower 6 is controlled at 75-85°C.
[0093] The outlet temperature of the primary circulating condenser 9 is controlled to be 40°C.
[0094] The outlet temperature of the primary product condenser 11 is controlled to be 35°C.
[0095] The temperatur...
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