Alkyl benzene sulfonic acid discoloring process
A technology of alkylbenzene sulfonic acid and process, which is applied in the field of low-color alkylbenzene sulfonic acid products, and can solve problems such as inability to meet decolorization requirements, large color difference, and reduction of dark-colored alkylbenzene sulfonic acid color.
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Embodiment 1
[0016] Enter 3 tons of 35klett alkyl benzene sulfonic acid into the reaction kettle to maintain the temperature of the material at 45±5°C, add 1% by weight of alkyl benzene sulfonic acid, decolorizing agent activated clay, that is, 30 kg, stir to react 0.5 After hours, the stirring was stopped, the unloading centrifuge was turned on, and the reacted alkylbenzene sulfonic acid was input for separation. The finished product of alkylbenzene sulfonic acid was about 2.995 tons, the loss was about 5 kg, and the residue was about 35 kg. The color of benzenesulfonic acid is 12klett. The loss rate ratio of the decolorizing agent is 0.17%:1%=0.17. Based on the current market price of alkylbenzene sulfonic acid of 12,000 yuan per ton, the method of the present invention increases the processing cost by about 40 yuan per ton. Combined with energy consumption, the cost will increase by about 0.4%, which is fully acceptable to general enterprises.
Embodiment 2
[0018] Enter 3 tons of 42klett alkyl benzene sulfonic acid into the reaction kettle to maintain the temperature of the material at 45±5°C, add 2% of the weight of alkyl benzene sulfonic acid, decolorizing agent activated clay, that is, 60 kg, and stir for 1 After hours, the stirring was stopped, the unloading centrifuge was turned on, and the reacted alkyl benzene sulfonic acid was input for separation. The finished product of alkyl benzene sulfonic acid was about 2.988 tons, the loss was 12 kg, and the residue was about 72 kg. The color of sulfonic acid is 12klett. The loss rate is 0.4%: 2%=0.20 compared with the decoloring agent, and the processing cost per ton is increased by about 88 yuan by adopting the method of the present invention. Combined with energy consumption, the increase in cost is about 0.86%, which is fully acceptable to general enterprises.
Embodiment 3
[0020] Enter 3 tons of alkylbenzene sulfonic acid with a color of 45klett into the reactor to maintain the temperature of the material at 45±5°C, and add 3% by weight of alkylbenzene sulfonic acid as a decolorizing agent activated clay, which is 90 kg, and stir for 1 After hours, the stirring was stopped, the unloading centrifuge was turned on, and the reacted alkylbenzene sulfonic acid was input for separation. The finished product of alkylbenzene sulfonic acid was about 2.985 tons, the loss was about 22 kg, and the residue was about 112 kg. The color of benzenesulfonic acid is 14klett. The loss rate is 0.73%: 2%=0.243 than the decoloring agent, and the processing cost per ton is increased by about 148 yuan by adopting the method of the present invention. Combined with energy consumption, the increase in cost is about 1.36%, which is fully acceptable to general enterprises.
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