Method for separating 2,3-butanediol

A butanediol, fully mixed technology, applied in chemical instruments and methods, separation/purification of hydroxyl compounds, preparation of organic compounds, etc., can solve problems such as affecting purification, increasing production costs, environmental pollution, etc. Reduce, increase concentration, realize the effect of recycling

Active Publication Date: 2016-06-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The comprehensive application of water phase separation and extraction separation technology is beneficial to improve the separation effect of 2,3-butanediol, but in the process, a large amount of inorganic salts will be added to reduce the hydrophilicity of 2,3-butanediol
A large amount of inorganic salts introduced in the two-phase aqueous phase process, a small amount of inorganic salts will remain in the 2,3-butanediol organic extract, affecting its further purification, most of which will exist in the water phase, increasing production costs, and pollute the environment

Method used

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  • Method for separating 2,3-butanediol
  • Method for separating 2,3-butanediol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] (1) Aqueous two-phase extraction: Take 2L of the fermentation broth, add 400g of sodium acetate, mix well, add 500mL of butanol, mix well and let stand.

[0032] (2) Electrodialysis desalination:

[0033] A. Take 600 mL of supernatant liquid obtained by two-phase extraction and perform electrodialysis. When the conductivity is less than 100 μS / cm, collect the supernatant liquid and concentrated liquid I to obtain 200 mL of concentrated liquid I.

[0034] B. Take 2300 mL of the lower phase clear liquid obtained by two-phase extraction and perform electrodialysis. When the conductivity is <300 μS / cm, collect the dope III to obtain 800 mL of dope III.

[0035] (3) Rectification: The clear liquid obtained in step (2) A was subjected to atmospheric distillation, and the butanol fraction was collected at 118°C, and the 2,3-butanediol fraction was collected at 180°C.

[0036] Results: 131mL of 2,3-butanediol was evaporated at about 180℃; the total recovery rate of 2,3-butaned...

Embodiment 2

[0038] (1) Aqueous two-phase extraction: Take 4L of the fermentation clear liquid, add 1200g of potassium succinate, mix well, add 1500mL of oleyl alcohol, mix well and let stand.

[0039](2) Electrodialysis desalination:

[0040] A. Take 1630 mL of supernatant liquid obtained by two-phase extraction for electrodialysis. When the conductivity is <100 μS / cm, collect the supernatant liquid and dope I.

[0041] B. Take 4350mL of the lower phase clear solution obtained by two-phase extraction for electrodialysis, and use the concentrated solution I as the electrodialysis circulating fluid. When the conductivity is <300μS / cm, collect 2400mL of the concentrated solution II.

[0042] (3) Rectification: The clear liquid obtained in step (2) A was subjected to atmospheric distillation, and the 2,3-butanediol fraction was collected at 180°C, and no salt components were separated out of the still residue.

[0043] Results: 240mL of 2,3-butanediol was evaporated at about 180℃; the total ...

Embodiment 3

[0045] (1) Aqueous two-phase extraction: Take 2L of the fermentation clear liquid, add 20mL of concentrated solution I and 800mL of concentrated solution III in step (2) in Example 1, and add 1000mL of butanol, mix well and let stand.

[0046] (2) Electrodialysis desalination:

[0047] A. Take 1300 mL of the supernatant liquid obtained by two-phase extraction for electrodialysis, and when the conductivity is <100 μS / cm, collect the supernatant liquid and concentrated liquid I.

[0048] B. Take 2300 mL of the lower phase clear liquid obtained by the two-phase extraction and perform electrodialysis. When the conductivity is <300 μS / cm, collect the concentrated liquid III.

[0049] (3) Rectification: The clear liquid obtained in step (2) A was subjected to atmospheric distillation, and the butanol fraction was collected at 118°C, and the 2,3-butanediol fraction was collected at 180°C.

[0050] Results: 128mL of 2,3-butanediol was evaporated at about 180℃; the total recovery rate...

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Abstract

The invention discloses a method for separating 2,3-butanediol. The method comprises the following steps: (1) carrying out pretreatment on fermentation broth, so as to obtain clear fermentation broth; (2) adding an inorganic salt and/or an organic acid salt into the clear fermentation broth, carrying out thorough mixing, then, adding a low-polarity organic substance into the clear fermentation broth, carrying out thorough mixing, and then, carrying out standing layering, so as to obtain an upper phase, i.e., a 2,3-butanediol organic solution and a lower phase, i.e., a salt solution; and (3) carrying out electrodialysis desalination treatment on the upper phase, i.e., the 2,3-butanediol organic solution, and collecting a clear solution and concentrated liquor I; and carrying out electrodialysis desalination treatment on the lower phase, i.e., the salt solution by taking the concentrated liquor I as electrodialysis concentrated liquor circulating liquid, collecting and recycling concentrated liquor II, and distilling the clear solution, thereby obtaining the 2,3-butanediol product. According to the method, biomacromolecules such as thallus dissolved protein and lipids can be effectively removed from the fermentation broth so as to form a relatively uniform and pure liquid-phase system, and the implementation of next-step refining manners such as double-aqueous-phase and rectifying is facilitated, so that the method is applicable to large-scale production application.

Description

technical field [0001] The invention belongs to the field of biochemical industry, in particular to a method for separating 2,3-butanediol from fermentation liquid. Background technique [0002] 2,3-Butanediol is a potential bulk chemical. As an important chemical raw material and liquid fuel, it can be widely used in chemical industry, food, fuel, aerospace and other fields. The combustion value of 2,3-butanediol is comparable to that of ethanol and methanol. It is one of the potential liquid fuels and can also be used as a fuel additive. The dehydration product of 2,3-butanediol, methyl ethyl ketone, is also an important chemical raw material, widely used in industries such as fuel, paint, binder, lubricant, and ink. 2,3-butanediol is also used as a flavor additive, which can be added to liquor in an appropriate amount to make the taste mellow; diacetyl obtained by catalytic dehydrogenation is a high-value food additive; acetoin (3- Hydroxy-2-butanone, Acetoin) is a natu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C29/86C07C29/74C07C31/20
Inventor 樊亚超张霖廖莎姚新武孙启梅
Owner CHINA PETROLEUM & CHEM CORP
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