Technical process of preparing high-purity L-lactic acid
A process method and high-purity technology, applied in the refining field of high-purity L-lactic acid, can solve the problems of excessive impurities, reduced distillation efficiency and productivity, and inability to achieve, optimize short-path distillation technology, improve extraction yield, and recover Take advantage of convenient effects
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Embodiment 1
[0031] Embodiment 1 (three-stage short-path distillation)
[0032]Send 50 liters of the decolorized and separated L-lactic acid (content 60%) solution into a thin-film concentration evaporator, and carry out decompression concentration under the conditions of a vacuum of 0.8-0.9Mpa and a temperature of 70°C to obtain L-lactic acid The solution was concentrated to 95%. Through the method of vacuum suction, the feed liquid is sucked into the feed tank, kept at 60-70°C, and at a flow rate of 6 liters / hour, it enters the first-stage short-path distiller with an evaporation area of 0.1M2. Under the conditions of 400Pa and jacket temperature of 80°C, the chromaticity of the primary heavy component product is 220 AAPHA, the water collected in the cold trap is 1.2 liters (acid content 10%), the chromaticity of the light component is 20 APHA, and the L-lactic acid content is 99 %, the collection volume is 0.3 liters. The primary heavy component material is sent into the secondary s...
Embodiment 2
[0035] Embodiment 2 (secondary short path distillation)
[0036] Send 100 liters of L-lactic acid (content 30%) solution after membrane treatment into a thin-film concentration evaporator, and carry out decompression concentration under the condition of vacuum degree of 0.8-0.9Mpa and temperature of 70°C, to L-lactic acid solution Concentrated to 95%. Through the method of vacuum suction, the feed liquid is sucked into the feed tank, kept at 60-70°C, and at a flow rate of 6 liters / hour, it enters the first-stage short-path distiller with an evaporation area of 0.1M2. Under the conditions of 400Pa and jacket temperature of 70°C, the chromaticity of the primary heavy component product is 1500 AAPHA, the water collected in the cold trap is 1.2 liters (acid content 10%), the chromaticity of the light component is 15 APHA, and the L-lactic acid content is 99 %, the collection volume is 0.3 liters. The primary heavy component material is sent into the secondary short path distil...
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