Process for recovery of carboxylic acids from the waste salt sol

Chemistry of carbon compounds – Miscellaneous organic carbon compounds – C-metal

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260484R, 260485R, 260488F, 260535R, 260537P, 260540, 260541, 260542, C07C 5144, C07C 5148

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active

039694658

ABSTRACT:
Waste salt solution from cyclohexanone manufacture is acidulated in a neutralizer, after which the organic phase is separated and subjected to a counter-current extraction with a saturated aqueous solution of mostly monocarboxylic acids separated from a later stage of the process. The watery extract carries off sodium sulphate that would otherwise interfere with further refining and this extract is then returned to the neutralizing vessel where the waste salt solutions are being acidulated, thereby reducing the need for externally supplied water to keep sodium sulphate from precipitating in the neutralizer and also enabling the dissolved monocarboxylic acids to be recovered. The organic phase leaving the counter-current extractor then goes to a flash evaporator in a condition now free of sodium sulphate, so that the evaporator may continuously remove water and monocarboxylic acids, which are then condensed and separated, with the water phase going back to the extractor as previously mentioned. The outputs are a mixture of monocarboxylic acids from the last separator and a mixture of dicarboxylic acids and hydroxy acids from the liquid coming out of the evaporator.

REFERENCES:
patent: 2714118 (1955-07-01), Copenhaver et al.
patent: 2859154 (1958-11-01), Othmer

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