Method for simultaneously producing lactic acid and alcohol or biogas from cereals
A process for the continuous production of lactic acid (a first fermentation product) and of a second fermentation product selected from the group consisting of alcohols and biogas, may include starting from the milling, necessarily carried out under dry conditions, of cereals and more particularly of corn. In the context of this process, a main flow and a flow of wastes which are difficult to ferment are recovered from the milling. These two flows are treated separately but simultaneously so as to produce, by fermentation, on the one hand, lactic acid and, on the other hand, an alcohol and/or biogas.
1. A continuous process for the simultaneous production of lactic acid and of a second fermentation product starting from cereals, the process comprising:
dry milling cereals using a mill to form a milled product;
recovering the milled product and mixing it in a mixer with a stream of water to create a slurry;
subjecting the slurry to a saccharification in a reactor and producing a crude dextrose stream;
separating, in a separator, the crude dextrose stream into a first flow comprising a liquid flow and a second flow comprising solid part;
removing an oil resulting from the milling and occurring in the liquid flow for subsequent treatment, and recovering a purified dextrose flow;
producing a fermentation product in the form of a lactic acid by subjecting the purified dextrose flow to a selective separation of sugars to recover a purified flow and a flow rich in oligosaccharides, before subjecting the purified flow to a fermentation in the presence of a microorganism appropriate for producing the lactic acid;
recovering the solid dextrose flow via a first pipe containing products which are difficult to ferment, and recovering the flow rich in oligosaccharides via a second pipe, to hydrolyze contents of the first and second pipes in a reactor under hydrolysis conditions and to convert the contents into a fermentable dextrose flow; and
subjecting the fermentable dextrose flow to a fermentation in a fermenter to produce a second fermentation product.
2. The process as claimed in claim 1 , wherein the selective separation of the sugars from the purified dextrose flow is carried out by chromatography.
3. The process as claimed in claim 1 , wherein the hydrolysis in the reactor is carried out in the presence of a strong acid at a temperature of between 140 and 180° C., for a period of 30 minutes to 2 hours.
4. The process as claimed in claim 1 , wherein the second fermentation product is selected from the group consisting of an alcohol and a biogas.
5. The process as claimed in claim 4 , wherein the alcohol is ethanol or butanol.
6. The process as claimed in claim 1 , wherein the cereals are selected from the group consisting of corn kernels and cobs.
7. The process as claimed in claim 1 , wherein the microorganism is selected from the group consisting of Saccharomyces, Schizosaccharomyces, Zymomonas mobilis , Clostridia, Escherichia coli or Pseudomonasputida.
8. A system for continuously producing, simultaneously, two dextrose streams starting from a dry milling of cereals, the system comprising:
a grain mill equipped for a dry milling;
a mixing vessel configured to prepare a slurry resulting from mixing of a milled product from the grain mill with a stream of water;
a saccharification reactor;
a first separator configured to produce two dextrose flows from the crude dextrose stream, a first flow containing a liquid matter, and a second flow containing a solid matter;
a second separator configured to remove oil from the first flow containing the liquid matter, and to recover a purified dextrose flow;
a system for separation by chromatography to remove oligosaccharides from the purified dextrose flow;
a first fermenter configured to produce lactic acid; and
a second fermenter configured to produce an alcohol or a biogas.