The present invention is related to sustainable fermentation processes with increased efficiency and less environmental impact. Particularly, the present invention is related to a process wherein in one fermentation process two or more fermentation products can be produced and isolated, i.e. a “primary” fermentation product and a “secondary” fermentation product, particularly wherein one is a water soluble organic compound and one is a fat-soluble organic compound particularly a fat-soluble vitamin, preferably vitamin K2.

The present invention is related to sustainable fermentation processes with increased efficiency and less environmental impact. Particularly, the present invention is related to a process wherein in one fermentation process two or more fermentation products can be produced and isolated, i.e. a “primary” fermentation product and a “secondary” fermentation product, particularly wherein one is a water soluble organic compound and one is a fat-soluble organic compound particularly a fat-soluble vitamin, preferably vitamin K2.

Controlled coenzyme Q.sub.10 (CoQ.sub.10) fermentation production processes and methods for controlling the CoQ.sub.10 fermentation production processes are provided in the present disclosure. The processes may include growing a microbial culture of bacteria by providing a carbon source and an oxygen source for a predetermined period of time, thereby producing CoQ.sub.10-containing bacteria, carbon dioxide, and lactate in the bacterial culture. During various stages of the production process, the concentration of carbon dioxide may be maintained at predetermined levels, respectively. Alternatively or additionally, during various stages of the production process, the concentration of lactate may be maintained at predetermined levels, respectively.

The disclosure discloses construction of recombinant Saccharomyces cerevisiae for synthesizing carminic acid and application thereof and belongs to the technical field of genetic engineering and bioengineering. The disclosure obtains recombinant S. cerevisiae CA-B2 capable of synthesizing carminic acid by heterologously expressing cyclase Zhul, aromatase ZhuJ, OKS of Octaketide synthase 1, C-glucosyltransferase UGT2, monooxygenase aptC and 4′-phosphopantetheinyl transferase npgA in S. cerevisiae. The recombinant S. cerevisiae can be used for synthesizing carminic acid by taking self-synthesized acetyl-CoA and malonyl-CoA as a precursor. On this basis, OKS, cyclase, aromatase, C-glucosyltransferase and monooxygenase relevant to carminic acid are integrated to a high copy site, which can remarkably improve the yield of carminic acid. The yield of carminic acid can be increased to 2664.6 .Math.g/L by optimizing fermentation conditions, and the fermentation time is shortened significantly. Therefore, the recombinant S. cerevisiae plays an important role in the fields of cosmetics, textiles and food.

The use of a cytochrome P-450 enzyme comprising SEQ ID NO: 110, or a variant enzyme having at least 70% identity thereto and having CYP-450 activity, for the hydroxylation of an organic compound, wherein the amino acid residue at position 291 is not threonine.

The use of a cytochrome P-450 enzyme comprising SEQ ID NO: 110, or a variant enzyme having at least 70% identity thereto and having CYP-450 activity, for the hydroxylation of an organic compound, wherein the amino acid residue at position 291 is not threonine.

Controlled coenzyme Q.sub.10 (CoQ.sub.10) fermentation production processes and methods for controlling the CoQ.sub.10 fermentation production processes are provided in the present disclosure. The processes may include growing a microbial culture of bacteria by providing a carbon source and an oxygen source for a predetermined period of time, thereby producing CoQ.sub.10-containing bacteria, carbon dioxide, and lactate in the bacterial culture. During various stages of the production process, the concentration of carbon dioxide may be maintained at predetermined levels, respectively. Alternatively or additionally, during various stages of the production process, the concentration of lactate may be maintained at predetermined levels, respectively.

The present invention relates to a process for preparing a compound having the formula (I), said process comprising the following steps: a) the addition of an oxygen source into a solution of a compound of formula (II), in a water-miscible solvent, b) the addition of a laccase in the solution obtained after step a); and c) the possible recovering of the compound of formula (I) thus obtained.

##STR00001##

The present invention relates to a process for preparing a compound having the formula (I), said process comprising the following steps: a) the addition of an oxygen source into a solution of a compound of formula (II), in a water-miscible solvent, b) the addition of a laccase in the solution obtained after step a); and c) the possible recovering of the compound of formula (I) thus obtained.

##STR00001##

Provided is a Bacillus subtilis natto strain ST-1008, deposited under the accession number CGMCC No. 17894. Also provided is a method for producing MK-7. The method comprises: culturing the Bacillus subtilis natto strain of CGMCC No. 17894 in a culture medium so as to produce MK-7 in the strain cell and the culture medium, and recovering and purifying MK-7 from the strain cell and the culture medium. Also provided are a MK-7 preparation, a MK-7 pure premix, and a pure MK-7.