Aqueous fermentation feedstock and a method for the production thereof
Aqueous fermentation feedstock and method of producing same. The feedstock includes glucose and dextrose oligomers, wherein (i) glucose concentration is in a range between 10 gram/Liter (g/L) and 150 g/L; (ii) dextrose oligomers concentration is in a range between 50 g/L and 300 g/L; and optionally (iii) slurried particles of less than 0.5 micron; (iv) slurried particles of more than 0.5 micron, wherein a content of such suspended particles of more than 0.5 micron is less than 30 g/L; (v) ash at a concentration in a range between 20 g/L and 50 g/L; (vi) lactate at a concentration in a range between 0.5 g/L and 10 g/L; (vii) protein at a concentration in a range between 5 g/L and 50 g/L; (viii) corn oil at a concentration of less than 10 g/L; and/or (ix) glycerol at a concentration in a range between 1 g/L and 30 g/L.
1. An aqueous bacterial fermentation feedstock comprising glucose and dextrose oligomers, wherein
(i) glucose concentration is in the range between 10 gram/Liter (g/L) and 150 g/L;
(ii) dextrose oligomers concentration is in the range between 50 g/L and 300 g/L; and
(iii) less than 30 g/L of slurried starch particles having a size of more than 0.5 micron; and
at least one selected from the group consisting of:
(iv) slurried starch particles of less than 0.5 micron;
(v) ash at a concentration in the range between 20 g/L and 50 g/L;
(vi) lactate at a concentration in the range between 0.5 g/L and 10 g/L;
(vii) protein at a concentration in the range between 5 g/L and 50 g/L;
(viii) corn oil at a concentration of less than 10 g/L; and
(viii) glycerol at a concentration in the range between 1 g/L and 30 g/L.
2. The aqueous bacterial fermentation feedstock of claim 1 , characterized by being sterile.
3. A method for producing said aqueous bacterial fermentation feedstock of claim 1 , comprising
(i) providing corn kernels;
(ii) comminuting said corn kernels to form comminuted corn kernels;
(iii) forming an aqueous slurry of said comminuted corn kernels;
(iv) treating said slurry with alpha-amylase enzymes and optionally also with gluco-amylase, at a temperature greater than 150 degrees Fahrenheit, whereby a corn mash is formed, wherein said corn mash comprises water soluble carbohydrates and water-insoluble carbohydrates;
(v) filtering at least a fraction of said corn mash as a filtration feed on a microfiltration membrane comprising sintered stainless steel with a ceramic coating comprising titanium dioxide, wherein said filtering is characterized by at least one of:
(a) feed, permeate and retentate temperature ranging between 100 and 210 degrees Fahrenheit;
(b) feed pressure ranging between 2 and 10 atmospheres gauge;
(c) retentate pressure ranging between 2 and 10 atmospheres gauge;
(d) permeate pressure ranging between 1 and 8 atmospheres gauge;
(e) circulation or feed flow rate that creates a linear velocity within the membranes of at least 5 feet per second; and
(f) transmembrane pressure drop ranging between 1 and 10 atmospheres gauge;
whereby an aqueous filtration permeate, comprising said water-soluble carbohydrates, and a filtration retentate comprising said water-insoluble carbohydrates, are formed; and
(vi) separating said filtration permeate from said filtration retentate, to form separated permeate and separated retentate.
4. The method of claim 3 , wherein the duration of said treating with alpha-amylase enzymes is in the range between 30 minutes and 30 minutes.
5. The method of claim 3 , wherein said treating further comprises grinding of said slurry.
6. The method of claim 3 , wherein said treating further comprises jet-cooking of said slurry.
7. The method of claim 3 , wherein said microfiltration membrane is characterized by porosity in the range between 0.01 micron and 0.5 micron.
8. A method for the production of bacterial single-cell protein, comprising culturing selected bacteria in an aqueous fermentation feedstock according to claim 1 .
9. An integrated method for the production of bacterial single-cell protein and ethanol, comprising fermenting said water-soluble carbohydrates in said separated permeate of claim 3 to form bacterial single cell protein and fermenting said water-insoluble carbohydrate in said separated retentate of claim 3 to form ethanol.