Pro-fragrance compounds
    71.
    发明授权

    公开(公告)号:US10752862B2

    公开(公告)日:2020-08-25

    申请号:US15631647

    申请日:2017-06-23

    申请人: FIRMENICH SA

    摘要: A compound is provided of Formula (I) wherein R1 represents a C3 to C20 hydrocarbon group derived from an alcohol of formula R1OH, from a formate of formula R1OCH═O, or a cinnamyl aldehyde of Formula (II) wherein a compound of Formula I is capable of releasing a compound, when oxidized, selected from the group consisting of a fragrant alcohol of formula R1OH, a fragrant formate ester of formula R1OCH═O and aryl aldehyde of Formula (III) wherein R2 is, independently, hydrogen atom, hydroxyl group, optionally substituted C1-C6 alkyl group, C1-C6 alkoxy group, or —O(C═O)CH(CH3)2 wherein any two of R2 may form an optionally substituted 5 or 6 membered ring. The compounds are useful for example as a precursor for the prolonged delivery or release of fragrant compounds such as fragrant alcohols, fragrant aldehydes or fragrant formates.

    Mild and selective vanadium-catalyzed oxidation of benzylic, allylic, and propargylic alcohols using air
    75.
    发明授权
    Mild and selective vanadium-catalyzed oxidation of benzylic, allylic, and propargylic alcohols using air 有权
    使用空气对苄型,烯丙基型和炔丙醇进行温和选择性钒催化氧化

    公开(公告)号:US08519132B2

    公开(公告)日:2013-08-27

    申请号:US13414975

    申请日:2012-03-08

    IPC分类号: C07F9/00 C07C45/37

    摘要: The invention concerns processes for oxidizing an alcohol to produce a carbonyl compound. The processes comprise contacting the alcohol with (i) a gaseous mixture comprising oxygen; and (ii) an amine compound in the presence of a catalyst, having the formula: where each of R1-R12 are independently H, alkyl, aryl, CF3, halogen, OR13, SO3R14, C(O)R15, CONR16R17 or CO2R18; each of R13-R18 is independently alkyl or aryl; and Z is alkl or aryl.

    摘要翻译: 本发明涉及氧化醇以产生羰基化合物的方法。 该方法包括使醇与(i)包含氧的气​​体混合物接触; 具有下式的催化剂存在下的胺化合物:其中R 1 -R 12各自独立地为H,烷基,芳基,CF 3,卤素,OR 13,SO 3 R 14,C(O)R 15,CONR 16 R 17或CO 2 R 18; R13-R18各自独立地为烷基或芳基; Z是烷基或芳基。

    Process for producing acetone from bioethanol
    76.
    发明授权
    Process for producing acetone from bioethanol 有权
    从生物乙醇生产丙酮的方法

    公开(公告)号:US07973199B2

    公开(公告)日:2011-07-05

    申请号:US12868018

    申请日:2010-08-25

    IPC分类号: C07C45/29 C07C45/37

    摘要: The present invention provides a technique for producing acetone in a high yield from hydrated ethanol derived from biomass, without requiring a large amount of energy. Hydrated ethanol derived from biomass is heated to a reaction temperature of 400° C. or higher in the presence of a Zr—Fe catalyst, thereby producing acetone. The reaction temperature is preferably from 450 to 550° C., and the Zr—Fe catalyst preferably contains 5 to 10% by mass of Zr. The present invention allows purification of hydrated acetone without requiring purification of the hydrated ethanol.

    摘要翻译: 本发明提供了从生物质得到的水合乙醇以高产率生产丙酮的技术,而不需要大量的能量。 在Zr-Fe催化剂的存在下,将来自生物质的水合乙醇加热至400℃以上的反应温度,从而生成丙酮。 反应温度优选为450〜550℃,Zr-Fe催化剂优选含有5〜10质量%的Zr。 本发明允许水合丙酮的纯化,而不需要纯化水合乙醇。

    Catalytic gas phase oxidation reaction
    80.
    发明申请
    Catalytic gas phase oxidation reaction 有权
    催化气相氧化反应

    公开(公告)号:US20050090695A1

    公开(公告)日:2005-04-28

    申请号:US10958015

    申请日:2004-10-04

    摘要: An object of the present invention is to provide a catalytic gas phase oxidation reaction in which: even under reaction conditions of a higher gas pressure, a higher concentration of the raw material gas and a larger space velocity of a reaction gas, the thermal accumulation at the hot spot portion can be sufficiently suppressed with ease and at low costs, so that the reaction can be continued for a long time while a high yield is maintained. As a means of achieving this object, a catalytic gas phase oxidation reaction according to the present invention is a catalytic gas phase oxidation reaction with molecular oxygen or a molecular-oxygen-containing gas by using a fixed-bed multitubular reactor packed with catalysts; with the catalytic gas phase oxidation reaction being characterized in that: a catalyst-packed layer of each reaction tube of the reactor is divided into at least two reaction zones in a tubular axial direction; and the packing of the catalysts is such that the occupation volumes of the catalysts differ between at least two of the reaction zones and that an inert substance molding is mixed in at least one of the reaction zones.

    摘要翻译: 本发明的目的是提供一种催化气相氧化反应,其中即使在较高气体压力,较高浓度的原料气体和较大的反应气体的空间速度的反应条件下,热累积在 可以容易地且低成本地充分地抑制热点部分,使得反应可以长时间持续,同时保持高产率。 作为实现该目的的手段,本发明的催化气相氧化反应是使用填充有催化剂的固定床多管反应器进行与分子氧或含分子氧气体的催化气相氧化反应, 催化气相氧化反应的特征在于:将反应器的每个反应管的催化剂填充层分成至少两个沿管轴方向的反应区; 并且催化剂的填充使得催化剂的占有体积在至少两个反应区之间不同,并且惰性物质模制品在至少一个反应区中混合。