Reduction of non-starch polysaccharides and alpha-galactosides in soy flour by means of solid-state fermentation using cellulolytic bacteria isolated from different environments
US-9497980-B2 · Nov 22, 2016 · US
US10136661B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10136661-B2 |
| Application number | US-201514708918-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 11, 2015 |
| Priority date | May 9, 2014 |
| Publication date | Nov 27, 2018 |
| Grant date | Nov 27, 2018 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
An improved method for producing fermented soybean meal which performs fermentation process and drying process separately in the production of the fermented soybean meal. The method for preparing fermented soybean meal enables prevention of contamination by various germs while shortening the time required for its preparation compared to the conventional method. Therefore, the method can be widely used to more economically prepare the fermented soybean meal.
Opening claim text (preview).
What is claimed is: 1. A method for preparing fermented soybean meal, comprising: (a3) fermenting soybean meal in a fermentation apparatus while adding water to the fermenting the soybean meal to maintain moisture content in the range of 40-60%; (a4) pre-drying the fermented soybean meal to achieve a moisture content to 25 to 32%; in a pre-drying apparatus; (b) eddycurrent-transferring the pre-dried fermented soybean meal to a drying apparatus from the pre-drying apparatus using an eddycurrent-transferring apparatus; and (c) drying the fermented soybean meal in the drying apparatus at a temperature of from 75 to 90° C. for from 10 to 35 minutes. 2. The method of claim 1 , wherein step (a) comprises (a1) adding water to the soybean meal followed by heat-treatment; (a2) inoculating the heat-treated soybean meal with a fermenting microorganism; and (a3) fermenting the soybean meal inoculated with the fermenting microorganism on a solid medium to obtain the fermented soybean meal. 3. The method of claim 2 , wherein during the during pre-drying step (a4) the soybean meal temperature is adjusted to 25-30° C. 4. The method of claim 2 , wherein step (a1) is performed by treating with steam at from 70 to 130° C. or superheated steam at from 200 to 300° C. 5. The method of claim 2 , which further comprises cooling the soybean meal to from 30 to 50° C. between step (a1) and step (a2). 6. The method of claim 2 , wherein step (a2) is performed by inoculating the soybean meal with the fermenting microorganism selected from the group consisting of Lactobacillus sakei, Lactobacillus brevis, Lactobacillus plantarum, Bacillus subtilis, Bacillus cereus, Bacillus megaterium, Bacillus clausii and a combination thereof. 7. The method of claim 2 , wherein step (a2) is performed by inoculating the soybean meal with the fermenting microorganism so that the number of cells of the microorganism contained in the soybean meal becomes 10 5 to 10 9 CFU/g. 8. The method of claim 2 wherein step (a3) is performed by fermenting the soybean meal at a temperature of from 20 to 50° C. for from 12 to 72 hours. 9. The method of claim 1 , wherein the moisture content of the fermented soybean meal is adjusted by applying a hot air of from 70 to 80° C. for from 60 to 90 minutes. 10. The method of claim 1 , wherein the step (c) is performed by a multi-chamber type continuous drying apparatus. 11. The method of claim 1 , wherein a final moisture content of the fermented soybean meal is from 3.9 to 10%. 12. The method of claim 10 , wherein the multi-chamber type continuous drying apparatus is a drying apparatus partitioned into three zones (zone # 1 , # 2 and # 3 ), includes a heater pipe per each zone as an auxiliary heat source, and controlling the temperature of each zone. 13. The method of claim 12 , wherein, when the multi-chamber type continuous drying apparatus is used, the drying is performed by maintaining the fermenting material temperature of zone # 1 at from 68 to 76° C.
for ruminants · CPC title
by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass · CPC title
Human Necessities · mapped topic
Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof (preservation thereof A23B75/00) · CPC title
Human Necessities · mapped topic
Related publications grouped by family.
Answers are generated from the same data shown on this page.