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1. 发明申请

US20090074941A1 Dewaxing 有权
标题翻译：脱蜡
公开(公告)号：US20090074941A1
公开(公告)日：2009-03-19
申请号：US12207481
申请日：2008-09-09
申请人： Andrew Finn , Alan Gabelman
发明人： Andrew Finn , Alan Gabelman
IPC分类号： C11B9/02
CPC分类号： C11B9/022 , A23L27/13
摘要： A method of dewaxing a citrus oil by subjecting the oil to a filtration process, in which the oil is caused to flow parallel to a porous membrane during which process it is maintained at a temperature of less than about 11° C., said membrane having an average pore size of from about 0.05-5 micrometres. The method produces citrus oils that are dewaxed to an unusually high extent.
摘要翻译：一种通过对油进行过滤处理来使柑橘油脱蜡的方法，其中使油平行于多孔膜流动，在该过程中，将其保持在小于约11℃的温度，所述膜具有平均孔径为约0.05-5微米。该方法生产的柑橘油脱蜡至非常高的程度。

2. 发明授权

US09422506B2 Dewaxing 有权
标题翻译：脱蜡
公开(公告)号：US09422506B2
公开(公告)日：2016-08-23
申请号：US12207481
申请日：2008-09-09
申请人： Andrew Finn , Alan Gabelman
发明人： Andrew Finn , Alan Gabelman
IPC分类号： A23L1/222 , C12C7/16 , C12G1/08 , C12H1/08 , C11B9/02
CPC分类号： C11B9/022 , A23L27/13
摘要： A method of dewaxing a citrus oil by subjecting the oil to a filtration process, in which the oil is caused to flow parallel to a porous membrane during which process it is maintained at a temperature of less than about 11° C., said membrane having an average pore size of from about 0.05-5 micrometers. The method produces citrus oils that are dewaxed to an unusually high extent.
摘要翻译：一种通过对油进行过滤处理来使柑橘油脱蜡的方法，其中使油平行于多孔膜流动，在该过程中，将其保持在小于约11℃的温度，所述膜具有平均孔径为约0.05-5微米。该方法生产的柑橘油脱蜡至非常高的程度。

3. 发明授权

US5783429A Enzymatic oxidation of alcohols to aldehydes in a continuous reaction system 失效
标题翻译：醇在连续反应体系中的酶催化氧化成醛
公开(公告)号：US5783429A
公开(公告)日：1998-07-21
申请号：US728085
申请日：1996-10-09
申请人： Alan Gabelman , Gary A. Luzio
发明人： Alan Gabelman , Gary A. Luzio
IPC分类号： C12P7/24
CPC分类号： C12P7/24 , Y10S435/911 , Y10S435/921
摘要： A process for the enzymatic oxidation of alcohols to aldehydes in a continuous reaction series is disclosed utilizing crude cellular methanol oxidase and catalase produced by an acceptable organism such as those selected from the genera of Pichia, Hansenula, Candida and Torulopsis. The process maintains a steady-state aldehyde concentration whereby enzyme activity is promoted. In particular, the process has two reactors operating in series continuously producing a fermenter effluent containing growing, intact yeast cells at a cell concentration of about 0.5 to about 3% by weight of the effluent by continuous culture of the cells on a methanol carbon source, continuously introducing the effluent from the first reactor to the second reactor, adding an alcohol feed at about 0.2-10% w/w and oxygen to the second reactor, maintaining a steady-state aldehyde concentration in the reaction mixture, the concentration of residual alcohol being about 0.1-9% w/w by controlling the rates of introduction of effluent and alcohol feed.
摘要翻译：利用粗细胞甲醇氧化酶和由可接受的生物如由毕赤酵母，汉逊酵母属，假丝酵母属和Torulopsis属中选择的生物体产生的过氧化氢酶，公开了将醇类酶连续反应的酶氧化成醛的方法。该过程保持稳态醛浓度，从而促进酶活性。特别地，该方法具有串联连续生产含有生长的完整酵母细胞的发酵罐流出物的两个反应器，其浓度为流出物重量的约0.5至约3重量％，通过在甲醇碳源上连续培养细胞，将来自第一反应器的流出物连续引入第二反应器，向第二反应器中加入约0.2-10％w / w的乙醇进料和氧，保持反应混合物中的稳态醛浓度，残余醇的浓度通过控制流出物和醇饲料的引入速率约为0.1-9％w / w。

4. 发明授权

US5137736A Production of propionic acid salts by fermentation of lactates using selenomonas ruminantium 失效
标题翻译：通过使用硒单胞菌反刍动物发酵乳酸盐生产丙酸盐
公开(公告)号：US5137736A
公开(公告)日：1992-08-11
申请号：US803863
申请日：1991-12-09
申请人： David C. Eaton , Alan Gabelman
发明人： David C. Eaton , Alan Gabelman
IPC分类号： C12N1/38 , C12P7/52
CPC分类号： C12P7/52 , C12N1/38
摘要： A process for preparing the sodium or calcium salt of propionic acid, comprising fermenting with the bacterium Selenomonas ruminantium an aqueous medium containing corn steep liquor or soy peptone, lactic acid, carbon dioxide, and sodium hydroxide, calcium carbonate, or calcium hydroxide as a neutralizing agent, the said process providing a yield in the said medium of at least 1% of the salt of propionic acid.

5. 发明授权

US5593872A Enzymatic oxidation of alcohols to aldehydes in a continuous reaction system using Candida boidinii 失效
标题翻译：在使用念珠菌的连续反应系统中将醇酶化为醛
公开(公告)号：US5593872A
公开(公告)日：1997-01-14
申请号：US524911
申请日：1995-09-08
申请人： Alan Gabelman , Gary A. Luzio
发明人： Alan Gabelman , Gary A. Luzio
IPC分类号： C12P7/24
CPC分类号： C12P7/24 , Y10S435/921
摘要： A process for the enzymatic oxidation of alcohols to aldehydes in a continuous reaction series is disclosed utilizing crude cellular methanol oxidase and catalase produced by an acceptable organism. The process maintains a steady-state aldehyde concentration whereby enzyme activity is promoted and side reactions are eliminated.In particular, the process has two reactors operating in series continuously producing a fermenter effluent containing growing, intact Candida boidinii cells at a cell concentration of about 0.5 to about 3% by weight of the effluent by continuous culture of the cells on a methanol carbon source, continuously introducing the effluent from the first reactor to the second reactor, adding an alcohol feed at about 0.2-10% w/w and oxygen to the second reactor, maintaining a steady-state aldehyde and alcohol concentration in the reaction mixture, the concentration of residual alcohol being about 0.1-9% w/w by controlling the rates of introduction of effluent and alcohol feed.
摘要翻译：使用粗细胞甲醇氧化酶和由可接受的生物体产生的过氧化氢酶，公开了连续反应系列中将醇酶氧化成醛的方法。该方法维持稳态醛浓度，从而促进酶活性并消除副反应。特别地，该方法具有串联连续生产含有生长完整的假丝酵母假丝酵母细胞的发酵罐流出物的两个反应器，其浓度为流出物重量的约0.5至约3％，通过在甲醇碳源上连续培养细胞将来自第一反应器的流出物连续引入第二反应器，向第二反应器中加入约0.2-10％w / w的醇进料和氧气，保持反应混合物中的稳态醛和醇浓度，浓度的残留酒精为约0.1-9％w / w，通过控制流出物和醇进料的引入速率。

6. 发明授权

US5132217A Start-up of continuous butyric acid fermentor 失效
标题翻译：启动连续的丁酸发酵罐
公开(公告)号：US5132217A
公开(公告)日：1992-07-21
申请号：US803861
申请日：1991-12-09
申请人： Alan Gabelman
发明人： Alan Gabelman
IPC分类号： C12P7/40
CPC分类号： C12P7/40 , Y10S435/813 , Y10S435/842
摘要： A process for starting up the continuous production of butyric acid by fermentation of a medium containing a starting amount of a nutrient substrate and a microorganism that converts the nutrient into butyric acid, that avoids an excess of nutrient in the fermentation broth and comprises the steps of (1) fermenting in a fermentor in batch style an amount of the medium that is substantially less than the working volume of the fermentor until the amount of the nutrient not yet converted is no more than a small fraction of the starting amount, (2) adding medium to the fermentor without removing any of the fermentation broth, until it contains approximately its working volume, then, (3) while continuing the addition, removing the fermentation broth containing the butyric acid product at a continuous rate that maintains a constant volume of medium in the fermentor, and thereafter maintaining continuous operation of the fermentation.

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