1. A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps: and (3) performing blood sugar reduction treatment by adopting a microbial fermentation technology, and collecting mycoprotein and crude salt.

2. A method for reducing sugar and collecting salt of amino acid wastewater is characterized by comprising the following steps:

1) culturing Schizosaccharomyces japonicus: inoculating the Schizosaccharomyces japonicus seed solution into a Schizosaccharomyces japonicus fermentation culture medium according to the inoculation amount of 4-8%, shaking and culturing at 35 ℃ and 180rpm, monitoring the concentration of thalli in the fermentation solution, stopping fermentation when the concentration of the thalli reaches OD600=8, and collecting the Schizosaccharomyces japonicus fermentation solution;

2) culturing staphylococcus nepalensis: inoculating the staphylococcus nepalensis seed liquid into a staphylococcus nepalensis fermentation medium according to the inoculation amount of 6-12%, shaking and culturing at 34 ℃ and 180rpm, monitoring the concentration of thalli in fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid;

3) reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating Schizosaccharomyces japonicus fermentation broth according to the inoculation amount of 1%, culturing for 4-6h, inoculating staphylococcus nepalensis fermentation broth according to the inoculation amount of 1.5%, continuously culturing for 20-40h, heating to 70 ℃, adding 0.1-0.5 per mill of calcium lignosulphonate flocculant by weight, uniformly stirring, standing for 2-10h, filtering by a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at 80-90 deg.C to obtain ammonium sulfate crude salt.

3. The method according to claim 2, wherein the Schizosaccharomyces japonicus fermentation medium is: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

4. The method of claim 2, wherein the nipaler pellet fermentation medium is: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Background

In amino acid production, a large amount of waste water can be generated, the waste water has the characteristics of high COD, high sugar, high salt and the like, and the treatment technology is always a hotspot and a difficulty of research. The waste water treatment process generally comprises precipitation, adsorption, acid-base neutralization and biochemical treatment. The biochemical treatment needs microorganisms which are resistant to high COD, high sugar and high salt environments, single microorganisms are difficult to effectively and thoroughly carry out blood sugar reduction treatment on the amino acid wastewater, different strains are combined to easily generate antagonistic competition effects, the aim of compatibility symbiosis cannot be achieved, the functions of the single strains can be reduced, and the research and research on the compatibility of the strains is the technical problem which needs to be solved.

The prior patent technology of the applicant is also recorded for the research of the compatible combination of the strains for repairing the amino acid wastewater. Patent CN104891677A relates to a preparation process of a complex microbial inoculum for repairing amino acid fermentation wastewater, which comprises the following steps: step 1) preparing a carrier, step 2) preparing a compound bacterial liquid, step 3) preparing a compound algae liquid, and step 4) preparing a compound microbial inoculum, wherein the compound bacterial liquid and algae are included. Patent CN105039228A relates to a biological agent for treating monosodium glutamate wastewater, which is prepared by mixing aerobic denitrifying bacteria, bacillus, aspergillus niger, rhodococcus, alcaligenes faecalis, streptomyces erythreus and candida albicans with an adsorbent carrier. The microbial preparation contains various microbial components, the preparation process is complicated, and once pollution occurs, the whole process cannot be implemented.

Screening for suitable microbial agents is a difficult point. The composite microbial preparation as an organic whole has the possible mutual antagonism or mutual promotion effect among various bacterial strains, the various bacterial strains have the mutual interaction in function, and the total technical effect is not the simple sum of the effects of all the parts. The mutual antagonism or mutual promotion of the same compound microbial inoculum in different fermentation processes can not be expected. If only the strains with similar functions or complementary strains are simply mixed, mutual antagonism among the strains is likely to occur, and the effect of the complex microbial inoculum is influenced.

Disclosure of Invention

The invention aims to provide a method for reducing blood sugar and collecting salt of amino acid wastewater aiming at the defects of the traditional process.

In order to realize the purpose of the invention, the following technical scheme is adopted:

a method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps: and (3) performing blood sugar reduction treatment by adopting a microbial fermentation technology, and collecting mycoprotein and crude salt.

A method for reducing sugar and collecting salt of amino acid wastewater is characterized by comprising the following steps:

1) culturing Schizosaccharomyces japonicus: inoculating the Schizosaccharomyces japonicus seed solution into a Schizosaccharomyces japonicus fermentation culture medium according to the inoculation amount of 4-8%, shaking and culturing at 35 ℃ and 180rpm, monitoring the concentration of thalli in the fermentation solution, stopping fermentation when the concentration of the thalli reaches OD600=8, and collecting the Schizosaccharomyces japonicus fermentation solution;

2) culturing staphylococcus nepalensis: inoculating the staphylococcus nepalensis seed liquid into a staphylococcus nepalensis fermentation medium according to the inoculation amount of 6-12%, shaking and culturing at 34 ℃ and 180rpm, monitoring the concentration of thalli in fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid;

3) reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating Schizosaccharomyces japonicus fermentation broth according to the inoculation amount of 1%, culturing for 4-6h, inoculating staphylococcus nepalensis fermentation broth according to the inoculation amount of 1.5%, continuously culturing for 20-40h, heating to 70 ℃, adding 0.1-0.5 per mill of calcium lignosulphonate flocculant by weight, uniformly stirring, standing for 2-10h, filtering by a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at 80-90 deg.C to obtain ammonium sulfate crude salt.

Preferably, the fission yeast Schizosaccharomyces japonicus fermentation medium is: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Preferably, the nipaler grape ball fermentation medium is: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

The beneficial effects achieved by the invention mainly comprise but are not limited to the following aspects:

only two kinds of microorganisms are adopted for compatibility treatment, and the preparation process and the technology are relatively simple;

compared with single Schizosaccharomyces japonicus or staphylococcus nepalensis, the two microorganisms can rapidly reduce the sugar content and correspondingly greatly improve the mycoprotein;

compared with the single staphylococcus nepalensis, the combination of the staphylococcus nepalensis and other yeasts has the advantages that the blood sugar reducing rate is not obviously improved, even the speed is reduced, and the result shows that the staphylococcus nepalensis and other yeasts are not suitable for symbiotic culture and cannot achieve the effect of synergistic treatment.

The invention can quickly reduce blood sugar, can recover crude salt and mycoprotein, really realizes changing waste into valuable, and has multiple purposes.

Detailed Description

Those skilled in the art can modify the process parameters appropriately to achieve the desired results with reference to the disclosure herein. It is expressly intended that all such similar substitutes and modifications which would be obvious to one skilled in the art are deemed to be included in the invention. While the products and methods of this invention have been described in terms of preferred embodiments, it will be apparent to those of skill in the art that variations and modifications, or appropriate alterations and combinations, of the products and methods described herein may be made and utilized without departing from the spirit, scope, and spirit of the invention. For a further understanding of the present invention, reference will now be made in detail to the following examples.

Example 1

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing Schizosaccharomyces japonicus: schizosaccharomyces japonicus seed liquid (OD 600= 3) was inoculated into a fermentation medium at an inoculation amount of 5%, and the temperature was 35%Shaking and culturing at 180rpm, monitoring the concentration of thallus in the fermentation liquor, stopping fermentation when the thallus concentration reaches OD600=8, and collecting Schizosaccharomyces japonicus fermentation liquor; fermentation medium components: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Culturing staphylococcus nepalensis: inoculating a staphylococcus nepalensis seed solution (OD 600= 2) into a fermentation medium according to the inoculation amount of 10%, shaking and culturing at a temperature of 34 ℃ and a shaking table of 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid; fermentation medium components: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Fermentation wastewater:

COD2.89g/L, salt content 17.8% (by weight), and sugar content 3.41% (by weight).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating Schizosaccharomyces japonicus fermentation broth according to the inoculation amount of 1%, culturing for 5h, inoculating staphylococcus nepalensis fermentation broth according to the inoculation amount of 1.5%, continuously culturing for 24h, heating to 70 ℃, adding 0.2 per thousand weight parts of calcium lignosulphonate flocculant, uniformly stirring, standing for 3h, filtering through a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Example 2

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing Schizosaccharomyces japonicus: inoculating Schizosaccharomyces japonicus seed liquid (OD 600= 2.5) into fermentation medium according to 6%, shaking and culturing at 36 deg.C and 180rpm, monitoring thallus concentration in fermentation liquidStopping fermentation when OD600=11 is reached, and collecting Schizosaccharomyces japonicus fermentation liquor; fermentation medium components: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.5mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Culturing staphylococcus nepalensis: inoculating a staphylococcus nepalensis seed solution (OD 600= 2.8) into a fermentation culture medium according to the inoculation amount of 10%, performing shake culture on a shaking table at 180rpm at the temperature of 35 ℃, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=15, and collecting the staphylococcus nepalensis fermentation liquid; fermentation medium components: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Fermentation wastewater:

COD3.05g/L, salt content 18.4% (mass percent), and sugar content 3.45% (mass percent).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating Schizosaccharomyces japonicus fermentation broth according to the inoculation amount of 1%, culturing for 3h, inoculating staphylococcus nepalensis fermentation broth according to the inoculation amount of 1.5%, continuously culturing for 36h, heating to 70 ℃, adding 0.2 per thousand weight parts of calcium lignosulphonate flocculant, uniformly stirring, standing for 3h, filtering through a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Comparative example 1

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing Schizosaccharomyces japonicus: inoculating Schizosaccharomyces japonicus seed liquid (OD 600= 3) into a fermentation medium according to the inoculation amount of 5%, shaking and culturing at 35 ℃ and 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=8, and collecting the Schizosaccharomyces japonicus fermentation liquid; fermentation mediumThe components are as follows: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Fermentation wastewater:

COD2.89g/L, salt content 17.8% (by weight), and sugar content 3.41% (by weight).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating the fermentation broth of Schizosaccharomyces japonicus according to the inoculation amount of 2.5%, culturing for 30h, heating to 70 ℃, adding 0.2 per mill of calcium lignosulphonate flocculant by weight, uniformly stirring, standing for 3h, filtering by a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Comparative example 2

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing staphylococcus nepalensis: inoculating a staphylococcus nepalensis seed solution (OD 600= 2) into a fermentation medium according to the inoculation amount of 10%, shaking and culturing at a temperature of 34 ℃ and a shaking table of 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid; fermentation medium components: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Fermentation wastewater:

COD2.89g/L, salt content 17.8% (by weight), and sugar content 3.41% (by weight).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating 2.5% of an inoculum size into a staphylococcus nepalensis fermentation broth, culturing for 30h, heating to 70 ℃, adding 0.2 per mill of calcium lignosulphonate flocculant by weight, uniformly stirring, standing for 3h, filtering by a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Comparative example 3

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing saccharomyces cerevisiae: inoculating a saccharomyces cerevisiae seed solution (OD 600= 3) into a fermentation culture medium according to the inoculation amount of 5%, shaking and culturing at 35 ℃ and 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=8, and collecting the saccharomyces cerevisiae fermentation liquid; fermentation medium components: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Culturing staphylococcus nepalensis: inoculating a staphylococcus nepalensis seed solution (OD 600= 2) into a fermentation medium according to the inoculation amount of 10%, shaking and culturing at a temperature of 34 ℃ and a shaking table of 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid; fermentation medium components: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Fermentation wastewater:

COD2.89g/L, salt content 17.8% (by weight), and sugar content 3.41% (by weight).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating saccharomyces cerevisiae fermentation liquor according to the inoculation amount of 1%, culturing for 5h, inoculating staphylococcus nepalensis fermentation liquor according to the inoculation amount of 1.5%, continuously culturing for 24h, heating to 70 ℃, adding 0.2 per thousand parts by weight of calcium lignosulphonate flocculant, uniformly stirring, standing for 3h, filtering through a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Comparative example 4

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing rhodosporidium palustum: inoculating rhodosporidium palustre seed liquid (OD 600= 3) into a fermentation culture medium according to the inoculation amount of 5%, carrying out shaking culture on a shaking table at 180rpm at the temperature of 35 ℃, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=8, and collecting the rhodosporidium palustre fermentation liquid; fermentation medium components: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Culturing staphylococcus nepalensis: inoculating a staphylococcus nepalensis seed solution (OD 600= 2) into a fermentation medium according to the inoculation amount of 10%, shaking and culturing at a temperature of 34 ℃ and a shaking table of 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid; fermentation medium components: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Fermentation wastewater:

COD2.89g/L, salt content 17.8% (by weight), and sugar content 3.41% (by weight).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating rhodosporidium palustre fermentation liquor according to the inoculation amount of 1%, culturing for 5h, inoculating staphylococcus nepalensis fermentation liquor according to the inoculation amount of 1.5%, continuously culturing for 24h, heating to 70 ℃, adding 0.2 per thousand weight parts of calcium lignosulphonate flocculant, uniformly stirring, standing for 3h, filtering through a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Comparative example 5

A method for reducing sugar and collecting salt of amino acid wastewater comprises the following steps:

culturing pichia pastoris: inoculating a pichia pastoris seed solution (OD 600= 3) into a fermentation medium according to the inoculation amount of 5%, shaking and culturing at 35 ℃ and 180rpm in a shaking table, monitoring the concentration of thalli in fermentation liquor, stopping fermentation when the concentration of the thalli reaches OD600=8, and collecting the pichia pastoris fermentation liquor; fermentation medium components: taking 20g of glucose, 10g of corn steep liquor, 1g of potassium dihydrogen phosphate, 1g of dipotassium hydrogen phosphate, 0.01g of magnesium sulfate heptahydrate, 2mg of ferrous sulfate heptahydrate and VB₁Adding 0.1mg into the fermentation wastewater, stirring uniformly, adjusting pH to 6.5, and metering to 1L.

Culturing staphylococcus nepalensis: inoculating a staphylococcus nepalensis seed solution (OD 600= 2) into a fermentation medium according to the inoculation amount of 10%, shaking and culturing at a temperature of 34 ℃ and a shaking table of 180rpm, monitoring the concentration of thalli in the fermentation liquid, stopping fermentation when the concentration of the thalli reaches OD600=12, and collecting the staphylococcus nepalensis fermentation liquid; fermentation medium components: adding 12g of glucose, 8g of yeast powder, 2g of monopotassium phosphate, 2g of dipotassium phosphate, 0.02g of magnesium sulfate heptahydrate, 5mg of ferrous sulfate heptahydrate and 1mg of manganese sulfate monohydrate into the fermentation wastewater, uniformly stirring, adjusting the pH value to 6.5, and fixing the volume to 1L to obtain the finished product.

Fermentation wastewater:

COD2.89g/L, salt content 17.8% (by weight), and sugar content 3.41% (by weight).

Reducing blood sugar and collecting salt: adjusting the pH value of the fermentation wastewater to 6-7, inoculating pichia pastoris fermentation liquor according to the inoculation amount of 1%, culturing for 5h, inoculating staphylococcus nepalensis fermentation liquor according to the inoculation amount of 1.5%, continuously culturing for 24h, heating to 70 ℃, adding 0.2 per mill of calcium lignosulphonate flocculant by weight, uniformly stirring, standing for 3h, filtering through a plate frame, and collecting mycoprotein and filtrate; evaporating the filtrate by a multi-effect evaporator, and drying by a fluidized bed at the drying temperature of 80-90 ℃ to obtain the ammonium sulfate crude salt.

Example 3

Comparison before and after fermentation wastewater treatment

TABLE 1

Group of	COD g/L	Sugar content%	Dry weight g/L of mycoprotein
				Example 1	0.09	0.14	17.9
Comparative example 1	0.71	0.77	10.5
				Comparative example 2	0.48	0.56	12.8
Comparative example 3	0.83	0.98	9.9
				Comparative example 4	0.55	0.84	8.5
Comparative example 5	0.60	1.13	7.7

And (4) conclusion: compared with other yeast combinations, the hypoglycemic effect is better in example 1 of the invention, and the mycoprotein is correspondingly improved, which shows that the Schizosaccharomyces japonicus and the staphylococcus nepalensis can be symbiotically cooperated, and the COD and the hypoglycemic effect are obviously reduced after the other yeasts and the staphylococcus nepalensis are combined, which shows that the combination of the two strains has certain antagonism. Compared with single Schizosaccharomyces japonicus or staphylococcus nepalensis, the Schizosaccharomyces japonicus and the staphylococcus nepalensis are subjected to compatibility treatment together, so that the sugar content can be quickly reduced, and the mycoprotein is correspondingly and greatly improved.

Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the invention as defined by the appended claims.