Method for extracting 1,3-propylene glycol prepared from glycerin serving as biodiesel byproduct by resin adsorption
A technology of resin adsorption and propylene glycol, which is applied in the field of bioengineering, can solve the problems of membrane poisoning, high energy consumption of rectification, modification of coenzyme, etc., and achieve the effect of reducing waste water discharge, simple separation process, and suitable for industrialization
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Embodiment 1
[0016] (1) Biodiesel preparation and glycerin acquisition: For waste oil, acidified oil and other raw materials, the raw materials are pretreated with solid acid, the molar ratio of alcohol to oil is 6~12, the reaction temperature is about 100°C, and the reaction time is 3~5h. The acid value of raw materials such as oil and acidified oil is reduced to about 1mgKOH / g oil, and the alkali-catalyzed transesterification reaction is carried out. Catalyze the transesterification reaction to produce biodiesel, react for 2~4h, filter out the reaction solution, retain the solid base in the transesterification reactor for the next transesterification reaction, and settle the filtrate, the upper layer is the biodiesel phase, and distill under reduced pressure Evaporate excess methanol to obtain refined biodiesel (fatty acid methyl ester), and the lower layer is crude glycerin.
[0017] (2) Strain: the strain used for fermentation is Klebsiella, which is a facultative anaerobic bacterium, ...
Embodiment 2
[0025] (1) Biodiesel preparation and glycerol acquisition: same as in Example 1.
[0026] (2) bacterial classification is the same as example 1.
[0027] (3) culture medium is the same as example 1.
[0028] (4) Culture method: There are two types of seed culture and fermentation culture. The seed culture is carried out in a 500mL Erlenmeyer flask with a liquid volume of 100mL, a culture temperature of 30°C, a shaker speed of 200r / min, and aerobic culture for 20 hours; fermentation The culture was carried out in an automatic cell culture device with a working volume of 2 L, an actual filling volume of 1 L, an initial concentration of glycerol of 30 g / L, an inoculum size of 10%, a speed control of 200 r / min, and a nitrogen ventilation rate of 1 vvm. 2mol / L sodium hydroxide was used to adjust the pH to 7.0, the temperature was controlled at 37°C, and the fermentation was carried out for 24 hours.
[0029] (5) product separation: with embodiment 1.
[0030] The experimental re...
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