| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | APPARATUS AND METHOD FOR PRODUCING BIOBASED CARRIERS FROM BYPRODUCTS OF BIOMASS PROCESSING | US14939196 | 2015-11-12 | US20160135449A1 | 2016-05-19 | Klein E. Ileleji; Kyle V. Probst |
| An apparatus for producing biobased carriers for dispersal of biological and chemical molecules includes a premixer having a first inlet, a first outlet, a cavity configured for receiving a wet coproduct and a binder through the first inlet, and a stirring apparatus within the cavity for premixing the wet coproduct and binder into a substantially homogeneous mixture; a high shear mixer having a housing, a drive apparatus and a high shear apparatus, the housing defining an opening, the drive apparatus being within the housing and for forcing the substantially homogeneous mixture from the premixer into the high shear apparatus, and the high shear apparatus including a rotor, a stator and a screen covering the opening and being for shear mixing the mixture including forcing the mixture through the screen and out of the housing in the form of nucleation enhanced particles; and an agglomerator having an interior chamber sized and configured to receive the nucleation enhanced particles from the high shear mixer and for transforming the nucleation enhanced particles into substantially spherical biomass pellets. | ||||||
| 2 | ANIMAL FEED PRODUCT FOR MONOGASTRIC ANIMALS | EP14721867.1 | 2014-05-06 | EP3001794A1 | 2016-04-06 | MILOS, Klaudija |
| The present technology disclosed herein relates to animal feed compositions suitable for feeding monogastric animals comprising a high amount of distillers dried grains with solubles (DDGS) with improved nutrition quality, in particular DDGS with a reduced fiber content for a better availability and digestibility of the amino acids in the DDGS. Furthermore, animal feed compositions according to the present disclosure shows an excellent metabolizable energy (TME) value and energy associated with the carbohydrates, and are in particular useful for feeding poultry, in particular broilers directly after birth. | ||||||
| 3 | Apparatus and method for producing biobased carriers from byproducts of biomass processing | US14939196 | 2015-11-12 | US10051858B2 | 2018-08-21 | Klein E. Ileleji; Kyle V. Probst |
| An apparatus for producing biobased carriers for dispersal of biological and chemical molecules includes a premixer having a first inlet, a first outlet, a cavity configured for receiving a wet coproduct and a binder through the first inlet, and a stirring apparatus within the cavity for premixing the wet coproduct and binder into a substantially homogeneous mixture; a high shear mixer having a housing, a drive apparatus and a high shear apparatus, the housing defining an opening, the drive apparatus being within the housing and for forcing the substantially homogeneous mixture from the premixer into the high shear apparatus, and the high shear apparatus including a rotor, a stator and a screen covering the opening and being for shear mixing the mixture including forcing the mixture through the screen and out of the housing in the form of nucleation enhanced particles; and an agglomerator having an interior chamber sized and configured to receive the nucleation enhanced particles from the high shear mixer and for transforming the nucleation enhanced particles into substantially spherical biomass pellets. | ||||||
| 4 | Apparatus and method for producing biobased carriers from byproducts of biomass processing | US13106515 | 2011-05-12 | US09272468B1 | 2016-03-01 | Klein E. Ileleji; Kyle V. Probst |
| An apparatus for producing biobased carriers for dispersal of biological and chemical molecules includes a premixer having a first inlet, a first outlet, a cavity configured for receiving a wet coproduct and a binder through the first inlet, and a stirring apparatus within the cavity for premixing the wet coproduct and binder into a substantially homogeneous mixture; a high shear mixer having a housing, a drive apparatus and a high shear apparatus, the housing defining an opening, the drive apparatus being within the housing and for forcing the substantially homogeneous mixture from the premixer into the high shear apparatus, and the high shear apparatus including a rotor, a stator and a screen covering the opening and being for shear mixing the mixture including forcing the mixture through the screen and out of the housing in the form of nucleation enhanced particles; and an agglomerator having an interior chamber sized and configured to receive the nucleation enhanced particles from the high shear mixer and for transforming the nucleation enhanced particles into substantially spherical biomass pellets. | ||||||
| 5 | 動物飼料製造のための加水分解および発酵工程 | JP2014504395 | 2012-04-13 | JP5980903B2 | 2016-08-31 | ワーウィック・ライウッド; ジョン・ピンクニー; ムハンマド・ジャベド; ジェイムズ・エドワーズ |
| 6 | Hydrolysis and fermentation processes for animal feed production | JP2014504395 | 2012-04-13 | JP2014512816A | 2014-05-29 | ワーウィック・ライウッド; ジョン・ピンクニー; ムハンマド・ジャベド; ジェイムズ・エドワーズ |
| ａ）発酵原料または発酵原料に実施される発酵工程の非エタノール副産物の部分加水分解、この部分加水分解は非澱粉多糖類を可溶性オリゴマーおよびモノマーに変換する、ｂ）部分加水分解された原料または非エタノール副産物中のオリゴマーおよびモノマーを発酵してエタノールを生産する、ｃ）段階ｂ）の発酵段階からの非エタノール副産物を回収して、動物飼料製品、特に改良された栄養成分をもつ動物飼料製品を製造する、工程を含む、動物飼料製品生産の方法。 ａ）発酵原料に実施される発酵工程の非エタノール副産物の部分加水分解、この部分加水分解は非澱粉多糖類を可溶性オリゴマーおよびモノマーに変換する、ｂ）段階ａ）からの部分加水分解された製品を回収し、可溶性オリゴマーおよびモノマーを除去して、動物飼料製品、特に改良された栄養成分をもつ動物飼料製品を製造する、工程を含む、動物飼料製品生産の方法。 本方法は、減少したレベルのペントース糖、比較的増加したタンパク質濃度、比較的減少した繊維濃度、減少したレベルの可溶性オリゴマーおよびモノマー、または減少したレベルの還元糖、による、改良された栄養成分を持つ動物試料製品を生産する。 | ||||||
| 7 | COMPOSITIONS DERIVED FROM FERMENTATION PRODUCTS AND PROCESS OF MAKING SAME | EP13739329.4 | 2013-07-06 | EP2874502A1 | 2015-05-27 | REDFORD, Steven, G. |
| Feed compositions and methods of making feed compositions are disclosed herein. The feed compositions may include, on a dry weight basis, crude protein in an amount of about 40 wt% or greater, crude fat in an amount of up to about 20 wt%, neutral detergent fiber in an amount of up to about 20 wt%, and lysine in an amount of about 2.55 wt% or greater. The methods involve separating a beer composition produced by a starch-based feedstock-to-ethanol conversion, process into bulk solids and a fine solids, and removing liquid from the fine solids, in which the separating and removing are performed in a manner that reduces the total heat exposure of the fine solids as compared to processes relying on distillation to separate beer components and/or cooking to saccharify starch. | ||||||
| 8 | PROTEIN RECOVERY | EP12753541.7 | 2012-08-10 | EP2741615A2 | 2014-06-18 | WILLIAMS, Peter Edmond Vaughan |
| A process for recovering a proteinaceous material from a fermentable organic material, comprising: (i) forming an aqueous mixture of a fermentable organic material and a fermentation agent capable of fermenting the organic material to produce ethanol, wherein the organic material is a vegetable material containing protein; (ii) fermenting the aqueous mixture to produce ethanol; (iii) recovering from the fermented aqueous mixture an ethanol stream which is rich in ethanol and a co-product stream comprising unfermented organic material, fermentation agent and an aqueous solution of dissolved solids in water; (iv) subjecting the co-product stream to a first separation stage to recover a first stream rich in the unfermented organic material and a second stream rich in the fermentation agent suspended in the aqueous solution; and (v) subjecting the first stream to a protein recovery step in which at least part of the fibre in the unfermented organic material is separated from the unfermented organic material to provide a protein rich material and a residual fibre containing less protein than the rich material material. | ||||||
| 9 | HYDROLYSIS AND FERMENTATION PROCESS FOR ANIMAL FEED PRODUCTION | EP12716556.1 | 2012-04-13 | EP2696700A1 | 2014-02-19 | LYWOOD, Warwick; PINKNEY, John; JAVED, Muhammad; EDWARDS, James |
| A method for production of an animal feed product comprises: a) partial hydrolysis of a fermentation feedstock or the non-ethanol by-product of a fermentation process performed on a fermentation feedstock, which partial hydrolysis converts non starch polysaccharides to soluble oligomers and monomers; b) fermentation of the soluble oligomers and monomers in the partially hydrolysed feedstock or non-ethanol by-product to produce ethanol; e) recovery of the non-ethanol by-product from the fermentation of step b) to produce an animal feed product more specifically an animal feed product with improved nutritional content. A method for production of an animal feed product comprises: a) partial hydrolosis of the non ethanol by-product of a fermentation process performed on a fermentation feedstock, which partial hydrolysis converts non starch polysaccharides to soluble oligomers and monomers; b) recovery of the partially hydrolysed product from step a), to exclude the soluble oligomers and monomers, to produce an animal feed product, more specifically an animal feed product with improved nutritional content. The methods produce an animal feed product with improved nutritional content by virtue of decreased levels of pentose sugars, increased relative protein concentration, decreased relative fibre concentration, decreased levels of soluble oligomers and monomers or decreased levels of reducing sugars. | ||||||
| 10 | PROTEIN RECOVERY | PCT/GB2012000655 | 2012-08-10 | WO2013021161A3 | 2013-05-30 | WILLIAMS PETER EDMOND VAUGHAN |
| A process for recovering a proteinaceous material from a fermentable organic material, comprising: (i) forming an aqueous mixture of a fermentable organic material and a fermentation agent capable of fermenting the organic material to produce ethanol, wherein the organic material is a vegetable material containing protein; (ii) fermenting the aqueous mixture to produce ethanol; (iii) recovering from the fermented aqueous mixture an ethanol stream which is rich in ethanol and a co-product stream comprising unfermented organic material, fermentation agent and an aqueous solution of dissolved solids in water; (iv) subjecting the co-product stream to a first separation stage to recover a first stream rich in the unfermented organic material and a second stream rich in the fermentation agent suspended in the aqueous solution; and (v) subjecting the first stream to a protein recovery step in which at least part of the fibre in the unfermented organic material is separated from the unfermented organic material to provide a protein rich material and a residual fibre containing less protein than the rich material material. | ||||||
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