Method for improving use ratio of sulfonating agent
A technology of sulfonating agent and utilization rate, which is applied in the field of improving the utilization rate of sulfonating agent, can solve the problems of low utilization rate of sulfonating agent and high content of inorganic salt, so as to reduce the content, reduce the production of by-products, and reduce the loss of lye The effect of consumption
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Embodiment 1
[0013] The 270~510°C distillate in the refinery is mixed with dichloroethane at a ratio of 3:2 (mass ratio), sulfur trioxide is diluted with dichloroethane to a 25% solution, and 300 g of the prepared distillate is gradually added dropwise to the prepared Sulfur trioxide 285g, the acid solution obtained after sulfonation enters the stripping tower from the top, the dry air is preheated to 80° C., and enters the stripping tower from the bottom. The volume ratio of hot air and acid solution is 3:1. Then the acid gas containing sulfur trioxide from the stripping tower enters the bottom of the absorption tower, and the fresh distillate oil prepared by distillate and dichloroethane enters the top of the absorption tower, and the acid gas and the preparation The final distillate oil enters the absorption tower at a volume ratio of 5:1. Get 300g of distillate oil discharged from the bottom of the absorption tower, add dropwise 285g of 25% sulfur trioxide, then make the sulfonated aci...
Embodiment 2
[0016] Distillate oil at 310-520°C in refinery is mixed with dichloroethane at a ratio of 3:2 (mass ratio), sulfur trioxide is diluted with dichloroethane to a 25% solution, 300 g of distillate oil is added dropwise to 295 g of 25% sulfur trioxide , the acid liquid obtained after sulfonation enters the stripping tower from the top, and the dry air is preheated to 50°C and enters the stripping tower from the bottom, and the volume ratio of hot air to acid liquid is 20:1. Then the acid gas containing sulfur trioxide from the stripping tower enters the bottom of the absorption tower, and the fresh distillate oil prepared by distillate and dichloroethane enters the top of the absorption tower, and the acid gas and the preparation The volume ratio of the final distillate is 30:1. Take 300g of distillate oil discharged from the absorption tower, add 266g of 25% sulfonating agent dropwise, and then make the sulfonated acid liquid enter the stripping tower with the above parameters, a...
Embodiment 3
[0019] Distillate oil at 330-450°C in refinery is mixed with dichloroethane at 1:1 (mass ratio), sulfur trioxide is diluted with dichloroethane to a 25% solution, take 300g of distillate oil and gradually add 210g of 25% sulfur trioxide , the acid liquid obtained after sulfonation enters the top of the stripping tower, the dry air is preheated to 65°C and enters the stripping tower from the bottom, and the volume ratio of hot air and acid liquid is 10:1. Then the acid gas containing sulfur trioxide discharged from the stripping tower enters the bottom of the absorption tower, and the fresh distillate oil prepared by distillate and ethylene dichloride enters the top of the absorption tower, and the acid gas and the preparation The volume ratio of the distillate after is 15:1. Take 300g of distillate oil discharged from the absorption tower, add dropwise 200g of 25% sulfonating agent, and then make the sulfonated acid solution enter the stripping tower with the above parameters,...
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