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A kind of method for removing sulfate radical in lactic acid

A sulfate and lactic acid technology, applied in chemical instruments and methods, separation/purification of carboxylic acid compounds, carboxylate preparation, etc., can solve the problems of low utilization efficiency, heavy load of sulfate radical removal process, etc., and achieve the goal of reducing load Effect

Active Publication Date: 2021-01-22
武汉三江航天固德生物科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a method for removing sulfate radicals in lactic acid, which can effectively remove the sulfate radical content in lactic acid, and solve the problem that the sulfate radical removal process load of anion exchange resin is relatively large and the use efficiency is low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] After sulfuric acid and calcium lactate metathesis reaction, adopt belt vacuum filter to carry out rough filtration, 50 tons of separated lactic acid dilute solution (lactic acid content is 20wt%), wherein the content of calcium sulfate is 0.33wt%, heat preservation is transferred to reaction tank In, adjust solution temperature at 80-95 ℃, add 380 kilograms of barium hydroxide octahydrate under stirring, after stirring reaction 30 minutes, carry out fine filtration with plate and frame filter, filter calcium sulfate in the clear liquid lactic acid separated out. The content of barium sulfate is 0.03wt%, the clear liquid lactic acid enters the ion exchange process, and the isolated barium sulfate can be sold as a building material.

Embodiment 2

[0026] A method for removing sulfate radicals in lactic acid, comprising the following steps: in the production process of lactic acid fermented by the calcium salt method, after the metathesis reaction of sulfuric acid and calcium lactate, rough filtration, the filtrate is a lactic acid solution, a total of 100 tons, heated to 80 After -95°C, 850 kg of barium hydroxide octahydrate was added under stirring to carry out the reaction, and after 25 minutes, it was filtered and separated again to obtain calcium sulfate removed from the lactic acid. The content of calcium sulfate in the lactic acid solution before the reaction was 0.37%, and the content of calcium sulfate in the lactic acid solution after the reaction was 0.032%.

Embodiment 3

[0028] A method for removing calcium sulfate in lactic acid, comprising the following steps: in the production process of lactic acid fermented by the calcium salt method, after metathesis reaction of sulfuric acid and calcium lactate, carrying out rough filtration, the filtrate is a lactic acid solution, a total of 100 tons, heated to 85 After -90°C, 810 kg of barium hydroxide octahydrate was added under stirring to carry out the reaction, and after 35 minutes, it was filtered and separated again to obtain calcium sulfate removed from the lactic acid. The content of calcium sulfate in the lactic acid solution before the reaction is 0.35%, and the content of calcium sulfate in the lactic acid solution after the reaction is 0.035%.

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PUM

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Abstract

The invention discloses a method for removing sulfate radicals from lactic acid. The method comprises the following steps: sulfuric acid and calcium lactate undergo a metathesis reaction in the process of fermenting lactic acid by a calcium salt technology, the obtained solution is filtered to obtain a filtrate which is a lactic acid solution containing a small amount of sulfate radicals, barium hydroxide is added, a reaction is performed, and filtration is performed to separate barium sulfate in order to remove the sulfate radicals from the lactic acid. The method allows the removal rate of the sulfate radicals from the lactic acid to be about 90%, and the exchange load of anion resin is greatly reduced although the sulfate radical removal still needs anion resin exchange, so the servicecycle of an anion resin exchange column is prolonged by 1.9-2.1 times. The investment of the anion exchange column and anion resin is reduced by 2 / 3, the amount of liquid 30 wt% sodium hydroxide consumed by every ton of the finished lactic acid is reduced by 0.06 t, the amount of tap water consumed by every ton of the finished lactic acid is reduced by 2.6 t, the amount of pure water consumed by every ton of the finished lactic acid is reduced by 1.0 t, the yield of the fermented lactic acid increases by 2%, the amount of produced wastewater is reduced by 3.0 t, and the comprehensive benefit is increased by 220-240 yuan.

Description

technical field [0001] The invention belongs to the field of biochemical industry, and in particular relates to a method for removing sulfate radicals in lactic acid. Background technique [0002] Lactic acid, scientific name 2-hydroxypropionic acid, molecular formula CH 3 CHOHCOOH. It has a wide range of applications in food, medicine, cosmetics, textiles, agriculture and other industries. It is a renewable resource product and is irreplaceable in industrial applications. Among them, it is the most widely used as a food additive. At present, the production of domestic lactic acid is obtained by using glucose as raw material and fermenting it by calcium salt method. National standards limit the content of various inorganic salt impurities in finished lactic acid. Such as chloride ≤ 0.002%, sulfate ≤ 0.005%, iron salt ≤ 0.001%, etc. In order to make the finished lactic acid meet the specified standards, domestic manufacturing units all adopt the following basic productio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C51/42C07C51/41C07C59/08
CPCC07C51/412C07C51/42C07C59/08
Inventor 胡秋明谢剑宏张金彬徐仁义卢明宏
Owner 武汉三江航天固德生物科技有限公司
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