| 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 | 通过汽提塔萃取塔系统回收挥发性羧酸 | CN201080037832.0 | 2010-08-18 | CN102574766B | 2014-08-13 | 杰弗里·S·托兰; 布赖恩·福迪; 维贾伊·阿南德 |
| 一种用于从含挥发性羧酸的含水流中回收所述挥发性羧酸的方法，该方法包括以下步骤：(i)从所述含水流中汽提所述羧酸，所述含水流通过使用木质纤维素原料作为底物的转化工艺产生，所述汽提包括通过使所述含水流与蒸汽彼此逆流流动而使所述含水流与所述蒸汽接触，由此产生包含气化的羧酸和蒸汽的蒸气流和经汽提的含水流；(ii)通过使所述蒸气流与有机溶剂接触来用所述有机溶剂萃取所述气化的羧酸，以产生(a)包含所述有机溶剂和所述羧酸的料流，以及(b)至少基本不含所述羧酸的蒸汽，其中所述有机溶剂具有至少约150℃的常压沸点并且不溶于水；(iii)将来自步骤(ii)的所述蒸汽返回到汽提步骤(步骤i)以进一步从所述含水流中汽提所述羧酸；和(iv)分离所述羧酸与所述有机溶剂。 | ||||||
| 2 | 通过萃取蒸发回收挥发性羧酸 | CN201080037848.1 | 2010-08-18 | CN102574767A | 2012-07-11 | 杰弗里·S·托兰; 布赖恩·福迪; 维贾伊·阿南德; 达芙妮·瓦农 |
| 一种用于从含挥发性羧酸的含水流中回收挥发性羧酸的方法，包括以下步骤：(a)蒸发所述含水流以产生包含已气化的挥发性羧酸和水蒸气的蒸气流，所述含水流通过使用木质纤维素原料作为底物的转化工艺产生；(b)使所述蒸气流与有机溶剂接触，以萃取存在于所述蒸气流中的所述挥发性羧酸，由此产生包含所述有机溶剂和所述挥发性羧酸的液流以及水蒸气流，其中所述有机溶剂具有至少约150℃的常压沸点并且不溶于水；和(c)分离所述挥发性羧酸与所述有机溶剂。 | ||||||
| 3 | 一种高酸髙酯调味酒的生产方法 | CN201410629781.0 | 2014-11-10 | CN104357299A | 2015-02-18 | 周新虎; 陈翔; 赵星辉; 张春林; 谢杰; 甘广东 |
| 本发明公开了一种高酸髙酯调味酒的生产方法，属于酿酒技术领域。本发明以纯粮浓香型白酒酿造副产物尾水油状物(TOSL)生产高酸髙酯调味酒的方法。其步骤是：首先将采集的TOSL样品除尾水、除固体杂质精制，然后将精制的TOSL与高度食用酒精水溶液混匀，再将该混合溶液旋转蒸发，收集馏分，最后将馏分以纯净水降度即得高酸髙酯调味酒。本发明充分利用酿酒过程副产物，既能够提高基础酒品质，带来较好的经济效益，又能够减少酿酒过程废弃物排放，减轻环境压力，符合国家倡导的工业生产节能减排的大趋势，具有较好的社会效益。 | ||||||
| 4 | 从用于生产醇的谷物中分离高价值副产品的系统和方法 | CN201180065801.0 | 2011-12-05 | CN103347615B | 2017-04-12 | 李介英 |
| 本发明提供了一种从用于生产醇的谷物中分离高价值副产品，例如油和/或胚芽的系统和方法。在一种实施方式中，从用于生产醇的谷物中分离副产品的方法包括：将粉碎的谷物进行液化以提供含有纤维、蛋白质和胚芽的液化淀粉溶液。从液化淀粉溶液中分离胚芽。将分离的胚芽进行研磨，例如，研磨至颗粒尺寸小于50微米以释放油，从而提供胚芽/油混合物。然后，在发酵前，从胚芽/油混合物中分离油以获得油副产品。所述胚芽/油混合物的pH值可以调节至约8到约10.5，和/或加入细胞破壁酶或化学试剂以促进油从胚芽中释放。在一种实施方式中，油的产量高于1.0lb/Bu。 | ||||||
| 5 | 玉米粉组合物及生产方法 | CN201380010707.4 | 2013-02-21 | CN104244729A | 2014-12-24 | 史蒂文·G·雷德福 |
| 提供自谷物到乙醇发酵过程衍生的组合物以及制造组合物的方法。组合物可为通过下述生成的玉米粉产品，即通过将玉米粒分级以便分离胚乳，在低于150～180°F的温度下将胚乳中的淀粉转化成糖，将糖发酵，并分离出所得到的固体。固体可经受蛋白质提取过程，然后经受溶剂交换以便将水从固体中去除，并用更易挥发的化学品诸如乙醇取代水。然后在低于150-180°F的温度下干燥固体。所得到的玉米粉产品可包括量在从约31至约45％的蛋白质，多达约3％的脂肪，多达约3％的灰分，量在从约32至约50％的中性洗涤剂纤维，以及多达约15％的淀粉，所有都基于干重。 | ||||||
| 6 | 通过萃取蒸发回收挥发性羧酸 | CN201080037848.1 | 2010-08-18 | CN102574767B | 2014-05-07 | 杰弗里·S·托兰; 布赖恩·福迪; 维贾伊·阿南德; 达芙妮·瓦农 |
| 一种用于从含挥发性羧酸的含水流中回收挥发性羧酸的方法，包括以下步骤：(a)蒸发所述含水流以产生包含已气化的挥发性羧酸和水蒸气的蒸气流，所述含水流通过使用木质纤维素原料作为底物的转化工艺产生；(b)使所述蒸气流与有机溶剂接触，以萃取存在于所述蒸气流中的所述挥发性羧酸，由此产生包含所述有机溶剂和所述挥发性羧酸的液流以及水蒸气流，其中所述有机溶剂具有至少约150℃的常压沸点并且不溶于水；和(c)分离所述挥发性羧酸与所述有机溶剂。 | ||||||
| 7 | 从用于生产醇的谷物中分离高价值副产品的系统和方法 | CN201180065801.0 | 2011-12-05 | CN103347615A | 2013-10-09 | 李介英 |
| 本发明提供了一种从用于生产醇的谷物中分离高价值副产品，例如油和/或胚芽的系统和方法。在一种实施方式中，从用于生产醇的谷物中分离副产品的方法包括：将粉碎的谷物进行液化以提供含有纤维、蛋白质和胚芽的液化淀粉溶液。从液化淀粉溶液中分离胚芽。将分离的胚芽进行研磨，例如，研磨至颗粒尺寸小于50微米以释放油，从而提供胚芽/油混合物。然后，在发酵前，从胚芽/油混合物中分离油以获得油副产品。所述胚芽/油混合物的pH值可以调节至约8到约10.5，和/或加入细胞破壁酶或化学试剂以促进油从胚芽中释放。在一种实施方式中，油的产量高于1.0lb/Bu。 | ||||||
| 8 | 通过汽提塔萃取塔系统回收挥发性羧酸 | CN201080037832.0 | 2010-08-18 | CN102574766A | 2012-07-11 | 杰弗里·S·托兰; 布赖恩·福迪; 维贾伊·阿南德 |
| 一种用于从含挥发性羧酸的含水流中回收所述挥发性羧酸的方法，该方法包括以下步骤：(i)从所述含水流中汽提所述羧酸，所述含水流通过使用木质纤维素原料作为底物的转化工艺产生，所述汽提包括通过使所述含水流与蒸汽彼此逆流流动而使所述含水流与所述蒸汽接触，由此产生包含气化的羧酸和蒸汽的蒸气流和经汽提的含水流；(ii)通过使所述蒸气流与有机溶剂接触来用所述有机溶剂萃取所述气化的羧酸，以产生(a)包含所述有机溶剂和所述羧酸的料流，以及(b)至少基本不含所述羧酸的蒸汽，其中所述有机溶剂具有至少约150℃的常压沸点并且不溶于水；(iii)将来自步骤(ii)的所述蒸汽返回到汽提步骤(步骤i)以进一步从所述含水流中汽提所述羧酸；和(iv)分离所述羧酸与所述有机溶剂。 | ||||||
| 9 | Smoke point raiser | JP3441483 | 1983-03-04 | JPS59161492A | 1984-09-12 | FUKAZAWA TOYOJI; FUKAZAWA YOUJI |
| PURPOSE: A smoke point raiser that contains, as an active ingredient, a specifically heat-treated product of fruits, thus increasing combustion efficiency by adding a small amount of the product to gasoline, light oil, or heavy oil and preventing the engines, burners, stoves or the like from being stained and corroded. CONSTITUTION: Fruits, or their treated product, waste after fruits are squeezed or its fermentation product or its waste is heated under reflux at 60W100°C for 30W10hr in general, at some 100°C for 3hr preferably, and the product is subjected to extraction with an organic solvent such as petroleum ether, benzene, gasoline or light oil, when necessary. The heat treated product, preferably its extract with an organic solvent is used as the objective smoke point raiser. COPYRIGHT: (C)1984,JPO&Japio | ||||||
| 10 | 汚染軽減 | JP2016561748 | 2015-04-10 | JP2017513697A | 2017-06-01 | アダム・バーンフェルド; キース・エイチ・バーリュー; アンソニー・アール・カラブリア; ダンカン・コフィ; ベンジャミン・フックス; アナ・パウラ・ゴース; アダム・デイヴィッド・ヘンリー; ウォルター・タミュリス; ジョーセフ・ジェイ・ザハー |
| 本開示は、発酵または蒸留プロセスを実用する施設中の汚染を最小化するか、または低減させる方法、アプローチ、装置、設備、および系を対象とする。実施形態において、施設は、発酵産物、例えば、産物アルコール、例えば、ブタノールを産生するバイオ燃料プラントである。一部の実施形態において、方法、アプローチ、装置、設備、および系は、産物アルコールの産生において使用される材料と接触する設備の表面を含む設備を除染するための定置滅菌(SIP)軽減技術を含み得る定置清浄汚染(CIP)軽減技術を実用するように作動可能である。他の清浄および汚染最小化技術も記載される。 | ||||||
| 11 | JPS50134836A - | JP2793075 | 1975-03-07 | JPS50134836A | 1975-10-25 | |
| 12 | Method and apparatus for preventing environmental pollution due to alcohol | JP3417378 | 1978-03-27 | JPS54126670A | 1979-10-02 | FUJII TOSHIKATSU; IKUMOTO SHIGEHARU; SATAKE YASUHIRO; HATSUTORI NORIAKI |
| PURPOSE: To prevent propagation of bacteria which utilize alcohol preferentially, by arranging activated carbon fiber structures made from acrylonitrile type polymer in an exhaust gas path of a tank or a plant generating alcohol vapor to allow alcohol in exhaust gas to be adsorbed. CONSTITUTION: Support frame 14 housing activated carbon fiber structures 18 is put in slender box 4, fixed with flange 14, covered 5, and hermetically sealed. Exhaust gas in tank 1 is introduced from inlet 7 through valve 19 of pipe 2 into adsorber 3 perfectly isolated from the external atmosphere, and the gas is allowed to flow to the side of cover 5 through exhaust port 13. By being contacted to structures 18, the gas is filtered, and alcohol contained is thoroughly adsorbed. The resulting clean air reaches a pass at the opposite side of cover 5, and it is released from outlet 8. COPYRIGHT: (C)1979,JPO&Japio | ||||||
| 13 | ******** Sa * ke *** no *** no | JP655776 | 1976-01-22 | JPS5198380A | 1976-08-30 | |
| 14 | Method and arrangement for use with biochemical reactions | US561456 | 1975-03-24 | US3997405A | 1976-12-14 | Hans Muller; Felix Muller |
| Heat liberated during an exothermic biochemical reaction is utilized in carrying out an operation requiring energy such as drying the product obtained from the reaction or sterilizing the substrate used for the reaction. The liberated heat is absorbed by a vaporizable cooling medium for transfer to the operation requiring energy. Alternatively the temperature of the cooling medium subsequent to the absorption of heat thereby is raised by compressing the vaporized cooling medium. The heating cooling medium is used to carry out the operation requiring energy. An arrangement which includes a bioreactor is also disclosed and includes heat pump means for permitting utilization of heat liberated during an exothermic biochemical reaction in the performance of an operation requiring energy. | ||||||
| 15 | Process for lysing mycelial waste | US54299075 | 1975-01-22 | US3928642A | 1975-12-23 | HUBERT ALFRED W; RUSSELL RALPH T |
| Mycelial waste is lysed by subjecting the waste to a temperature of from about 140* to about 200*C. at a pressure of from the equilibrium pressure to about 2,000 p.s.i.g., and at a pH of from about 2 to about 10. The lysed mycelial waste is useful as an animal feed supplement.
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| 16 | Method of treating spent grain | US3721568D | 1970-07-14 | US3721568A | 1973-03-20 | WILSON J |
| THE SPENT GRAIN COMING FROM A STILL SPRAY DRIED IN A CONVENTIONAL SPRAY DRYER TO ARRIVE AT A DRIED GRAIN PRODUCT FIT FOR HUMAN CONSUMPTION OR SUBSTANTIALLY MITIGATE THE PROBLEMS OF POLLUTION CAUSED BY SPENT GRAIN CONSTITUENTS.
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| 17 | Process of producing ethyl acetate, ethyl alcohol and other products by fermentation | US23199027 | 1927-11-08 | US1866568A | 1932-07-12 | ALEXANDER IZSAK; MCDERMOTT FRANK A |
| 18 | 결합식 기화/스트리핑 흡수 모듈 | KR1020117027508 | 2010-04-16 | KR1020120007054A | 2012-01-19 | 맥그리거이안알.; 벨쳐스크리스토퍼에이취. |
| 본 발명의 공정에서 액체 혼합물 유동의 일부는 기화되어 증기 및 감손 액체 유동을 생성한다. 증기는, 증기로부터 하나 이상의 성분을 발열성으로 흡수하도록 구성된 브라인에 도입되고, 열이 배출되어, 적어도 열의 유동 및 상기 하나 이상의 성분이 강화된 브라인의 유동을 생성한다. 앞서 배출된 열은 전달되어 기화를 일으킨다. 이러한 열 전달은 작동 유체가 기체 상태로부터 액체 상태로 변화하는 것과 관련된다. 열 배출은 작동 유체가 액체 상태로부터 기체 상태로 변화하는 것을 수반한다. 액체 상태에서 작동 유체는 중력, 대류 및 위킹 중 하나 이상에 의해서만 유동한다. 기체 상태에서 작동 유체는 확산과 대류 중 하나 이상에 의해서만 유동한다.
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| 19 | Method and apparatus for efficiently dewatering corn stillage and other materials | US520409 | 1995-08-29 | US5662810A | 1997-09-02 | Ralph H. Willgohs |
| A new process and apparatus efficiently dewater aqueous solids residual after fermentation and distillation, such as corn stillage. The feed stream of aqueous solids slurry is fractionated into two or more sub-streams in such a way that one of the sub-streams contains predominately heavy particulate solids and has substantially improved free-draining characteristics. A second sub-stream contains lighter particles, entrained fines of the heavy particles, and a major portion of the liquid from the feed stream. The free-draining sub-stream is dewatered using a device such as a screen centrifuge or a screw press, both of which produce a cake of relatively high solids content. The remaining liquid from the feed stream is concentrated in an evaporator, before being mixed with the dewatered solids which may be dried to produce an animal feed. | ||||||
| 20 | Dewatering of distillery spent wash in the production of by product dreg meal | US3747758D | 1972-02-07 | US3747758A | 1973-07-24 | KERR R |
| The invention provides a method of and apparatus for recovering dissolved and suspended solids from a process for the production of grain whisky. The wort from a mashing tun or spent wash from distallation plant is fed on to a continuously moving filter screen in the form of a continuous belt. The wort or spent wash is fed on to the respective filter screen which moves at several hundred feet per minute so that a major portion of the liquid filters by gravity leaving on the screens a random dispersion of solids. The screens with the solids thereon are passed over or vacuum station for further dewatering and the dewatered solids are removed by adhesion to at least one roller where they are removed by centrifugal force into a hopper.
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