Process for the production of fatty alcohols
    1.
    发明授权
    Process for the production of fatty alcohols 失效
    生产脂肪醇的方法

    公开(公告)号:US5364986A

    公开(公告)日:1994-11-15

    申请号:US150931

    申请日:1993-11-10

    CPC分类号: B01J23/80 B01J8/06 C07C29/149

    摘要: C.sub.8-22 fatty alcohols are produced by a process which comprises contacting a triglyceride with hydrogen in the presence of a copper-zinc catalyst and in a reaction zone. The hydrogen pressure in the reaction zone is from about 200 to about 280 bar, the temperature of the entrance of the reaction zone is from about 200.degree. C. to about 230.degree. C., and the temperature of the exit of the reaction zone is from about 190.degree. C. to about 220.degree. C. The amount of 1,2-propanediol formed is optimized by the lower temperature of the exit portion of the reaction zone.

    摘要翻译: C8-22脂肪醇通过包括使甘油三酯与氢在铜 - 锌催化剂存在下和在反应区中接触的方法制备。 反应区中的氢气压力为约200至约280巴,反应区入口温度为约200℃至约230℃,反应区出口温度为 约190℃至约220℃。通过反应区的出口部分的较低温度优化形成的1,2-丙二醇的量。

    Method for producing alkyl-substituted butenols
    5.
    发明授权
    Method for producing alkyl-substituted butenols 有权
    烷基取代丁烯醇的制备方法

    公开(公告)号:US07169749B1

    公开(公告)日:2007-01-30

    申请号:US10088385

    申请日:2000-09-08

    IPC分类号: C07C27/22

    摘要: Alkyl-substituted butenols having the formula (I): R1—CH2—CH═CR2—CH2OH   (I) wherein R1 is a saturated or olefinically unsaturated alkyl or cycloalkyl group having from 4 to 16 carbon atoms and wherein R1 is optionally substituted by an alkyl, cycloalkyl, aryl or alkaryl having up to 12 carbon atoms; R2 is hydrogen or an alkyl group having from 1 to about 6 carbon atoms are produced by a process which comprises: (1) reacting an aldehyde of the formula (II): R1—CH2—CHO   (II) wherein R1 has the same meaning as in formula (I), with the corresponding lower aldehyde to form an unsaturated aldehyde in an inert organic solvent; (2) continuously contacting an optionally calcined copper/zinc catalyst with the unsaturated aldehyde under isothermal conditions at temperatures of from about 45 to about 60° C. and under a hydrogen pressure of from 1 to about 300 bar.

    摘要翻译: 具有式(I)的烷基取代的丁烯醇:<?in-line-formula description =“In-line formula”end =“lead”?> R SUB-CH-CR 2 -CH 2 OH(I)<βin-line-formula description =“In-line Formulas”end =“tail”?> 其中R 1是具有4至16个碳原子的饱和或烯属不饱和的烷基或环烷基,并且其中R 1任选被烷基,环烷基,芳基或烷芳基取代 具有多达12个碳原子; R 2是氢或具有1至约6个碳原子的烷基,其方法包括:(1)使式(II)的醛: 公式描述=“在线公式”end =“lead”?> R -CH 2 -CHO(II)<?in-line-formula description =“ 其中R 1具有与式(I)中相同的含义,其中相应的低级醛在惰性有机溶剂中形成不饱和醛; (2)在约45至约60℃的温度和1至约300巴的氢气压力的等温条件下,将任选煅烧的铜/锌催化剂与不饱和醛连续接触。

    Process for the production of fatty acid lower alkyl esters
    6.
    发明授权
    Process for the production of fatty acid lower alkyl esters 失效
    生产脂肪酸低级烷基酯的方法

    公开(公告)号:US5773636A

    公开(公告)日:1998-06-30

    申请号:US640921

    申请日:1996-08-05

    IPC分类号: C07C67/03 C11C1/00

    CPC分类号: C07C67/03

    摘要: A process for the production of fatty acid lower alkyl esters comprising the steps of: A) treating at least one fatty acid ester of glycerol with from about 0.3 to about 3% by weight, based on the weight of ester, of an acid at an elevated temperature; B) removing said acid from the treated fatty acid ester; and C) reacting the treated fatty acid ester with at least one lower aliphatic alcohol to transesterify the fatty acid ester.

    摘要翻译: 一种用于生产脂肪酸低级烷基酯的方法,包括以下步骤:A)以至少一种甘油脂肪酸酯的量处理至少一种脂肪酸酯,所述脂肪酸酯以约0.3至约3重量%(基于酯的重量计)的酸在 升温 B)从处理的脂肪酸酯中除去所述酸; 和C)使经处理的脂肪酸酯与至少一种低级脂族醇反应以酯交换脂肪酸酯。

    Process for the production of fatty acid lower alkyl esters
    7.
    发明授权
    Process for the production of fatty acid lower alkyl esters 失效
    生产脂肪酸低级烷基酯的方法

    公开(公告)号:US5455370A

    公开(公告)日:1995-10-03

    申请号:US178281

    申请日:1994-01-10

    CPC分类号: C11C3/04 C07C67/03

    摘要: Fatty acid glycerides can be transesterified with lower aliphatic alcohols if the reaction is carried out in the presence of fatty acids corresponding to formula (II):R.sup.2 --COOH (II),in which R.sup.2 is an aliphatic hydrocarbon moiety containing 11 to 17 carbon atoms and 0, 1 or 2 double bonds. The products are distinguished by a low content of bound glycerol and a low acid value. Removal or neutralization of the catalyst is unnecessary because, after the transesterification, the fatty acids are also present in the form of their esters.

    摘要翻译: PCT No.PCT / EP92 / 01463 Sec。 371日期1994年1月10日 102(e)日期1994年1月10日PCT提交1992年6月29日PCT公布。 出版物WO93 / 01263 如果反应在对应于式(II)的脂肪酸存在下进行,则其中R2是脂族烃(II),R2-COOH(Ⅱ) 部分含有11至17个碳原子和0,1或2个双键。 产品的特征在于低含量的结合甘油和低酸值。 催化剂的去除或中和是不必要的,因为在酯交换之后,脂肪酸也以它们的酯的形式存在。

    Process for the production of fatty acid esters of short-chain aliphatic
alcohols from fats and/or oils containing free fatty acids
    8.
    发明授权
    Process for the production of fatty acid esters of short-chain aliphatic alcohols from fats and/or oils containing free fatty acids 失效
    用于从含游离脂肪酸的脂肪和/或油生产短链脂族醇的脂肪酸酯的方法

    公开(公告)号:US4608202A

    公开(公告)日:1986-08-26

    申请号:US599090

    申请日:1984-04-11

    CPC分类号: C11C3/04

    摘要: For the production of fatty acid esters of short-chain, aliphatic alcohols by the catalytic transesterification of natural fats and/or oils containing free fatty acids (oil phase) with the corresponding monoalcohols, the oil phase is subjected to preliminary esterification with the monoalcohols in the presence of acidic esterification catalysts at temperatures no higher than 120.degree. C. and under pressures no higher than 5 bars and in the presence of a liquid entraining agent substantially immiscible with the oil phase, after which the reaction product is separated into an entraining agent phase containing the acidic catalyst and water of reaction and the treated oil phase, the oil phase is then subjected to transesterification while the acidic catalyst-containing entraining agent phase is returned, after at least partial drying, to the preliminary esterification stage. By this process, fats and/or oils with acid numbers of up to 60 can be processed in the preliminary esterification stage to give an oil phase having a low acid number.

    摘要翻译: 为了通过将含有游离脂肪酸(油相)的天然脂肪和/或油与相应的一元醇进行催化酯交换反应生产短链脂肪醇的脂肪酸酯,将油相用一元醇进行初步酯化 在不高于120℃的温度和不高于5巴的压力下和在与油相基本上不混溶的液体夹带剂的存在下,存在酸性酯化催化剂,然后将反应产物分离成夹带剂 含有酸性催化剂和反应水和处理油相的相,然后将油相进行酯交换反应,同时将酸性催化剂夹带剂相在至少部分干燥后返回到初步酯化阶段。 通过该方法,可以在初步酯化阶段处理酸值高达60的脂肪和/或油,得到酸值低的油相。