Method for extracting mycoprotein from liquid acetic acid fermentation tail liquid
A technology of bacterial protein and acetic acid fermentation, which is applied in the preparation methods of peptides, chemical instruments and methods, organic chemistry, etc., can solve the problems of low utilization rate of resources and difficult treatment of fermentation tail liquid, so as to improve the economic benefits of enterprises and reduce The difficulty of sewage treatment and the effect of improving resource utilization
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Embodiment 1
[0040] (1) Take the filtered liquid acetic acid fermentation tail liquid, transfer it to the tail liquid temporary storage tank, start the ceramic membrane filtration equipment, open the feed valve, return valve, liquid outlet valve, set the frequency of the booster pump to 60Hz, and start filtering , stop filtering when the filtration pressure rises to 0.4MPa from 0.2MPa, obtain the concentrated solution after filtering in the temporary storage tank, and obtain the concentrated tail liquid with a concentration ratio of 20%;
[0041] (2) The concentrated tail liquid obtained in step (1) is introduced into the heating device for circulation heating through a centrifugal pump, and after being heated by steam, when the temperature rises to 45° C., the discharge valve is opened to enter the pretreatment tank, and the discharge temperature is 50° C.;
[0042] (3) The concentrated tail liquid with a temperature of 50°C obtained in step (2) enters the high-speed jet flow dissolving de...
Embodiment 2
[0048] (1) Take the filtered liquid acetic acid fermentation tail liquid, transfer it to the tail liquid temporary storage tank, start the ceramic membrane filtration equipment, open the feed valve, return valve, liquid outlet valve, set the frequency of the booster pump to 60Hz, and start filtering , stop filtering when filter pressure rises to 0.4MPa by 0.2MPa, obtain the concentrated solution after filtering in the temporary storage tank, obtain the concentrated tail liquid that concentration ratio is 35%;
[0049] (2) The concentrated tail liquid obtained in step (1) is introduced into a heating device for circulation heating through a centrifugal pump. After heating by steam, when the temperature rises to 45° C., the discharge valve is opened to enter the pretreatment tank, and the discharge temperature is 55° C.;
[0050] (3) The concentrated tail liquid with a temperature of 55°C obtained in step (2) enters the high-speed jet flow dissolving device, and the booster pump ...
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