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1. 发明授权

US5001284A Process for manufacturing fatty alcohols 失效
标题翻译：制造脂肪醇的方法
公开(公告)号：US5001284A
公开(公告)日：1991-03-19
申请号：US420461
申请日：1989-10-12
申请人： Rene Dupont , Laurent Ferenczi , Guy Simonet
发明人： Rene Dupont , Laurent Ferenczi , Guy Simonet
IPC分类号： C01B3/32 , C07C29/149 , C07C29/136 , C07C31/04 , C07C31/125
CPC分类号： C07C29/149 , Y02P20/132
摘要： In a process for manufacturing fatty alcohols comprising hydrogenating the corresponding fatty acid methyl esters, the hydrogen used for the hydrogenation reaction is regenerated from impure methanol as a by-product of the reaction. The impure methanol recovered from the hydrogenation reactor is conducted to a steam reformer reactor, from whence the regenerated hydrogen is recycled back to the hydrogenation reactor.
摘要翻译：在制造脂肪醇的方法中，包括氢化相应的脂肪酸甲酯，用于氢化反应的氢气作为反应的副产物从不纯的甲醇中再生。将从氢化反应器回收的不纯的甲醇进行到蒸汽重整器反应器，从再生的氢再循环回加氢反应器。

2. 发明授权

US4986978A Process for reforming impure methanol 失效
标题翻译：重整不纯甲醇的方法
公开(公告)号：US4986978A
公开(公告)日：1991-01-22
申请号：US265299
申请日：1988-10-28
申请人： Rene Dupont , Guy Simonet
发明人： Rene Dupont , Guy Simonet
IPC分类号： C01B3/22 , B01J8/06 , C01B3/12 , C01B3/32
CPC分类号： C01B3/323
摘要： A method and apparatus are provided for reforming impure methanol wherein residual gas produced during the reforming reaction is combusted simultaneously with residual gas coming from the purification of the hydrogen produced. The apparatus includes a tubular reactor in which the steam reforming is performed, a vaporizer for the reaction mixture, a heat exchanger to exchange heat between the outgoing gases and the feed liquid, a separator, a purification unit, and a combustion furnace for the residual purification gas. The apparatus further comprises a pipe for bringing in the condensed water-alcohol mixture to the combustion furnace, this pipe being equipped with two heat exchangers.
摘要翻译：提供了一种用于重整不纯的甲醇的方法和装置，其中在重整反应期间产生的残余气体与来自生产的氢气的净化的残余气体同时燃烧。该装置包括管式反应器，其中进行蒸汽重整，用于反应混合物的蒸发器，用于在输出气体和进料液体之间交换热量的热交换器，用于残余物的分离器，净化单元和燃烧炉净化气体。该装置还包括用于将冷凝的水 - 醇混合物引入燃烧炉的管道，该管道装备有两个热交换器。

3. 发明授权

US4683294A Process for the extraction and purification of proteins from culture media producing them 失效
标题翻译：从产生它们的培养基中提取和纯化蛋白质的方法
公开(公告)号：US4683294A
公开(公告)日：1987-07-28
申请号：US719601
申请日：1985-04-03
申请人： Frans Van Wijnendaele , Daniel Gilles , Guy Simonet
发明人： Frans Van Wijnendaele , Daniel Gilles , Guy Simonet
IPC分类号： C12P21/00 , A61K39/29 , C07K1/14 , C07K1/36 , C07K14/02 , C12N1/06 , C12N15/00 , C12P21/02 , C12R1/865 , A61K39/12
CPC分类号： C07K14/005 , C07K1/303 , C07K1/36 , C12N1/063 , C12N2730/10122 , Y10S530/806
摘要： The process is applicable to the supernatant of engineered yeast cells disrupted in the presence of a non-ionic detergent: it comprises the precipitation of contaminants by polyethylene glycol and the treatment cation or, after eventual ultrafiltration, with ammonium sulfate.
摘要翻译：该方法适用于在非离子型洗涤剂存在下破碎的工程酵母细胞的上清液：其包括用聚乙二醇和处理阳离子沉淀污染物，或最终超滤后用硫酸铵沉淀。

4. 发明授权

US4981499A Process and plant for separating a gaseous mixture by adsorption 失效
标题翻译：用于通过吸附分离气体混合物的方法和设备
公开(公告)号：US4981499A
公开(公告)日：1991-01-01
申请号：US415444
申请日：1989-09-28
申请人： Leon Hay , Didier Crozel , Guy Simonet
发明人： Leon Hay , Didier Crozel , Guy Simonet
IPC分类号： B01D53/04 , B01D53/047 , C01B3/56 , C01B13/02 , C01B23/00
CPC分类号： B01D53/0476 , C01B13/0259 , C01B23/00 , C01B3/56 , B01D2256/12 , B01D2256/16 , B01D2256/18 , B01D2256/245 , B01D2257/102 , B01D2257/104 , B01D2257/11 , B01D2257/502 , B01D2257/504 , B01D2257/702 , B01D2259/4003 , B01D2259/40032 , B01D2259/40037 , B01D2259/40041 , B01D2259/40045 , B01D2259/40067 , B01D2259/40071 , B01D2259/40073 , B01D2259/40075 , B01D2259/404 , B01D2259/4061 , B01D2259/4062 , B01D53/053 , C01B2203/042 , C01B2203/0465 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2210/0046 , Y02C10/08 , Y02P20/152 , Y02P30/30
摘要： Process for separating a gaseous mixture by adsorption includes the steps of: (a) a cocurrent isobaric production (f.sub.p1 -f.sub.p2); (b) a pressure equalization between the adsorber undergoing decompression and another adsorber undergoing countercurrent recompression (f.sub.c1 -N.sub.4); (c) a cocurrent partial emptying to a reservoir (f); (d) a final countercurrent decompression (f.sub.a); (e) a countercurrent scavenging by the gas of the reservoir (f.sub.b); (f) a countercurrent partial recompression by at least one pressure equalization (f'.sub.e); (g) a countercurrent final recompression (f'.sub.di -F'.sub.d2); in which process the sum of the duration of the operations according to (c) and (d) is less than said phase shift and the sum of the durations of the operations according to (c), (d) and (e) is less than twice said phase shift; (h) at least two adsorbers are simultaneously in isobaric production, wherein: (i) the number of adsorbers is at least equal to four and less than 3+x+y, x and y being respectively the number of adsorbers in production and the number of pressure equalizations; (j) the emptying is introduced into the storage reservoir; (k) each pressure equalization is "direct".
摘要翻译：通过吸附分离气体混合物的方法包括以下步骤：（a）并流同质异位生产（fp1-fp2）; （b）进行减压的吸附器与进行逆流再压缩的另一吸附器之间的压力平衡（fc1-N4）; （c）同时部分排空到水库（f）; （d）最终逆流减压（fa）; （e）由储存器（fb）的气体逆流清除; （f）通过至少一个压力平衡（f'e）的逆流部分再压缩; （g）逆向最终重新压缩（f'di-F'd2）; 根据（c）和（d）的操作的持续时间的总和小于所述相移，并且根据（c），（d）和（e）的操作的持续时间之和小于此超过两倍的相移; （h）至少两个吸附器同时进行等压生产，其中：（i）吸附器的数量至少等于4和小于3 + x + y，x和y分别是生产中吸附器的数量，压力平衡数; （j）将排空物引入储存库; （k）每个压力均衡是“直接的”。

5. 发明授权

US4042349A Method of fractionation of a gaseous mixture by adsorption 失效
$Method of fractionation of a gaseous mixture by adsorption$
标题翻译：通过吸附分离气体混合物的方法
公开(公告)号：US4042349A
公开(公告)日：1977-08-16
申请号：US298774
申请日：1972-10-18
申请人： Yvonne Baudouin , Guy Simonet , Robert Eluard , Claude Pivard
发明人： Yvonne Baudouin , Guy Simonet , Robert Eluard , Claude Pivard
IPC分类号： B01D53/047 , B01D53/04
CPC分类号： B01D53/047 , B01D2253/104 , B01D2253/108 , B01D2253/116 , B01D2256/12 , B01D2256/16 , B01D2257/102 , B01D2257/11 , B01D2257/504 , B01D2257/80 , B01D2259/40007 , B01D2259/40015 , B01D2259/40032 , B01D2259/40052 , B01D2259/4006 , B01D2259/40064 , B01D2259/40066 , B01D2259/40067 , B01D2259/40081 , B01D2259/402 , B01D2259/404 , B01D2259/4141 , B01D53/0476 , B01D53/261 , Y02C10/08
摘要： An improved method of fractionation of a gaseous mixture by adsorption, in which the efficiency of extraction and the content of the desired constituent in the gaseous fraction extracted are increased, the method utilizing two or more adsorption lines, each including at least one adsorber comprising an adsorbent mass which preferentially adsorbs at least one constituent of the gaseous mixture, the first adsorption line comprising:A constant-pressure extraction stage, during which the gaseous mixture is introduced into the inlet of said line, circulates from the inlet to the outlet of at least one adsorber in said line in the adsorption direction, at a high pressure in said adsorber, so as to obtain at the outlet of said line a gaseous fraction impoverished in at least one constituent of said gaseous mixture;A regeneration stage comprising a period of falling pressure, during which the outlet of the adsorption line is closed and there is extracted at the inlet of said line a gaseous fraction enriched in at least one constituent of said gaseous mixture, while reducing the pressure in the adsorber to a low pressure for said adsorber;And a pressure-increase stage, during which the pressure in said adsorber is increased to the high pressure for said adsorber.The invention is applicable to any process of fractionation by adsorption and in particular to the purification of hydrogen from a steam re-forming unit.
摘要翻译：一种改进的通过吸附分离气体混合物的方法，其中萃取效率和提取的气体馏分中所需组分的含量增加，使用两种或多种吸附管线的方法，每种吸附管线包括至少一个吸附器，优选吸附气态混合物的至少一种组分的吸附剂质量，第一吸附管线包括：

6. 发明授权

US4066664A Intermediates for preparing .alpha.-carboxy-.alpha.-(3-thienyl)penicillin and cephalosporin derivatives 失效
标题翻译：制备“ - 三 - ” - （3-噻吩基）泼尼松和吡虫啉衍生物的中间体
公开(公告)号：US4066664A
公开(公告)日：1978-01-03
申请号：US727198
申请日：1976-09-27
申请人： Pierre Crooij , Guy Simonet
发明人： Pierre Crooij , Guy Simonet
IPC分类号： C07D499/46 , A61K31/43 , A61K31/545 , C07D20060101 , C07D333/24 , C07D499/12 , C07D499/44 , C07D499/72 , C07D499/74 , C07D501/06 , C07D501/20 , C07D501/22 , C07D501/26 , C07D501/36
CPC分类号： C07D501/20 , C07D499/72
摘要： A new process is disclosed for the preparation of alpha-carboxy-alpha-phenyl(or 3-thienyl)penicillin and cephalosporin derivatives.The process comprises reacting a 1.3-dioxane-4.6-dione derivative with the desired penicillanic or cephalosporanic acid derivative.

7. 发明授权

US4055625A Method of treatment of a mixture of air and at least partially radioactive rare gases 失效
标题翻译：处理空气和至少部分放射性稀有气体的混合物的方法
公开(公告)号：US4055625A
公开(公告)日：1977-10-25
申请号：US592949
申请日：1975-07-03
申请人： Pierre Faugeras , Pierre Lecoq , Pierre Miquel , Hubert Rouyer , Guy Simonet
发明人： Pierre Faugeras , Pierre Lecoq , Pierre Miquel , Hubert Rouyer , Guy Simonet
IPC分类号： C01B23/00 , F25J3/02 , G21F9/00 , G21F9/02
CPC分类号： C01B23/00 , F25J3/028 , G21F9/02 , F25J2205/82 , F25J2210/40 , F25J2215/34 , F25J2215/36 , F25J2215/42 , F25J2220/40 , Y02P20/152 , Y10S62/925
摘要： The method of treatment of a mixture of air and at least partially radioactive gases such as xenon and krypton in particular, especially gaseous effluents derived from the reprocessing of irradiated nuclear fuels, comprises a stage of concentration of the rare gases in solution in liquid oxygen by cryogenic distillation of the light gases and especially nitrogen from the liquefied mixture.
摘要翻译：特别是处理空气和至少部分放射性气体如氙气和氪气的混合物的方法，特别是衍生自经辐照的核燃料的后处理的气态流出物的方法包括通过以下方式浓缩液氧中溶液中的稀有气体的阶段：液化混合物中的轻质气体，特别是氮的低温蒸馏。

8. 发明授权

US4857317A Process for the extraction and purification of proteins from culture media producing them 失效
标题翻译：从产生它们的培养基中提取和纯化蛋白质的方法
公开(公告)号：US4857317A
公开(公告)日：1989-08-15
申请号：US42914
申请日：1987-04-27
申请人： Frans V. Wijnendaele , Daniel Gilles , Guy Simonet
发明人： Frans V. Wijnendaele , Daniel Gilles , Guy Simonet
IPC分类号： C12P21/00 , A61K39/29 , C07K1/14 , C07K1/36 , C07K14/02 , C12N1/06 , C12N15/00 , C12P21/02 , C12R1/865
CPC分类号： C07K14/005 , C07K1/303 , C07K1/36 , C12N1/063 , C12N2730/10122 , Y10S530/806
摘要： The process is applicable to the supernatant of engineered yeast cells disrupted in the presence of a non-ionic detergent; it comprises the precipitation of contaminants by polyethylene glycol and the treatment of this latter supernatant with either a bivalent metal cation or, after eventual ultrafiltration, with ammonium sulfate.
摘要翻译：该方法适用于在非离子型洗涤剂存在下破碎的工程酵母细胞的上清液; 它包括用聚乙二醇沉淀污染物，并用二价金属阳离子或最终超滤后用硫酸铵处理后一上清液。

9. 发明授权

US4649192A Method for the isolation and purification of hepatitis B surface antigen using polysorbate 失效
标题翻译：使用聚山梨酯分离和纯化乙型肝炎表面抗原的方法
公开(公告)号：US4649192A
公开(公告)日：1987-03-10
申请号：US739415
申请日：1985-05-30
申请人： Frans Van Wijnendaele , Guy Simonet
发明人： Frans Van Wijnendaele , Guy Simonet
IPC分类号： A61K39/29 , C07K14/02 , C07K3/18 , C07K3/28
CPC分类号： C07K14/005 , C12N2730/10122 , Y10S530/806 , Y10S530/808 , Y10S530/826
摘要： The supernatant of engineered yeast cells having produced hepatitis B surface antigaen and disrupted in the presence of a polysorbate non-ionic detergent is clarified by addition of urea and adsorbed on colloidal silica from which the purified antigen is desorbed with a low ionic strength buffer supplemented with urea and a polysorbate non-ionic detergent.
摘要翻译：产生乙型肝炎表面抗原并在聚山梨醇酯非离子型洗涤剂存在下破碎的工程酵母细胞的上清液通过添加尿素而被澄清，并吸附在胶体二氧化硅上，纯化的抗原用补充有尿素和聚山梨醇酯非离子型洗涤剂。

10. 发明授权

US4512778A Adsorption processes 失效
标题翻译：吸附过程
公开(公告)号：US4512778A
公开(公告)日：1985-04-23
申请号：US541082
申请日：1983-10-12
申请人： Guy Simonet , Leon Hay
发明人： Guy Simonet , Leon Hay
IPC分类号： B01D53/04 , B01D53/047
CPC分类号： B01D53/047 , B01D2259/4003 , B01D2259/40037 , B01D2259/40041 , B01D2259/40052 , B01D2259/40067 , B01D2259/40071 , B01D2259/40075 , B01D2259/4062 , B01D2259/4063 , B01D2259/4065 , B01D2259/4066
摘要： The gas originating from the expansion during the stage (T.sub.6) is directed into a buffer tank and each adsorber has an operating cycle delayed by 1/nth of the cycle period (T) with respect to a preceding one, and each production stage has a duration of (x/n)T, "n" being greater than or equal to 6, and "x" greater than or equal to 2, and each expansion stage at an intermediate pressure has a shorter duration than each elution stage.
摘要翻译：来自阶段（T6）期间的膨胀的气体被引导到缓冲罐中，并且每个吸附器具有延迟相对于前一循环周期（T）的1 / n的操作周期，并且每个生产阶段具有（x / n）T的持续时间，“n”大于或等于6，“x”大于或等于2，并且中间压力的每个膨胀级具有比每个洗脱阶段更短的持续时间。

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