Method for treating residual liquid after mother liquor distillation methanol recovery during production of sodium sulphoxylate by sodium formate process
A technology for sodium dithionite and methanol recovery, which is applied in the direction of thiosulfate/dithionite/polythionate, combustion methods, separation methods, etc., and can solve complex intermediate products, foul-smelling smoke, and difficult biochemical Handling and other issues
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no. 1 example
[0027] see figure 1 , the first embodiment of the present invention is realized according to the following steps:
[0028] Step 1, material concentration: the rectification raffinate 111 is obtained after the rectification of the mother liquor produced in the process of producing sodium dithionite by the sodium formate method to reclaim methanol, and the main component content of the rectification raffinate 111 is sodium formate 110g / l, sodium sulfite 8.9g / l l. Sodium thiosulfate 4.5g / l, methanol 6.5g / l, organic sulfide and other substances 61g / l, chemical oxygen demand (COD) 238000mg / l, take 10m 3 The above-mentioned rectification raffinate 111 is concentrated until a large amount of crystals appear, and the concentrated residue 112 in the form of a slurry is obtained after being released and cooled, with a weight of 2020 kg;
[0029] Step 2, incineration feeding stage: use the second-stage converter 121 to incinerate, use a heavy oil burner to first raise the temperature in...
no. 2 example
[0036] see figure 2 , the second embodiment of the present invention is realized according to the following steps:
[0037] Step 1, material concentration: the rectification raffinate 211 is obtained after the rectification of the mother liquor produced in the process of producing sodium dithionite by the sodium formate method to reclaim methanol, and the main component content of the rectification raffinate 211 is sodium formate 120g / l, sodium sulfite 7.8g / l l. Sodium thiosulfate 5.6g / l, methanol 5.8g / l, organic sulfide and other substances 63g / l, chemical oxygen demand (COD) 252000mg / l, take 10m 3 The above-mentioned rectification raffinate 211 is concentrated until a large amount of crystals appear to become a concentrated raffinate 213, and methanol is added to the concentrated raffinate 213 to filter out the crystal 214 with sodium formate and sodium sulfite as the main components to obtain a methanol leaching filtrate 215. The weight of the crystal 214 is 1120kg. Its m...
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