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    • 7. 发明授权
    • Method for producing alkoxyphenol and alkoxy-hydroxybenzaldehyde
    • 制备烷氧基苯酚和烷氧基 - 羟基苯甲醛的方法
    • US09334216B2
    • 2016-05-10
    • US14417015
    • 2013-07-12
    • RHODIA OPERATIONS
    • Laurent Garel
    • C07C45/38C07C51/353C07C41/06C07C41/16C07C51/367C07C45/54
    • C07C45/38C07C41/06C07C41/16C07C45/54C07C51/353C07C51/367Y02P20/582C07C43/23C07C59/64C07C47/58C07C47/575
    • The invention relates to a method for producing alkoxyphenol from hydroxyphenol, comprising an O-alkylation reaction of at least one hydroxyphenol into at least one alkoxyphenol, said reaction being carried out using an O-alkylating agent, an aqueous solvent containing a Bröensted base, and an organic solvent, with a base/O-alkylating agent ratio of between 0.5 and 1.5 in moles of base per mole of O-alkylating agent, an O-alkylating agent/hydroxyphenol ratio of between 0.5 and 2 moles of O-alkylating agent per mole of hydroxyphenol, and an organic solvent/hydroxyphenol ratio of less than 280 mL, preferably between 10 and 250 mL and more preferably still between 50 and 150 mL of organic solvent per mole of hydroxyphenol. The invention also relates to a method for producing at least one alkoxy-hydroxybenzaldehyde from at least one hydroxyphenol compound.
    • 本发明涉及一种由羟基苯酚生产烷氧基苯酚的方法,其中包括至少一种羟基苯酚与至少一种烷氧基苯酚的O-烷基化反应,所述反应使用O-烷基化试剂,含有布朗斯台德碱的含水溶剂和 一种有机溶剂,碱/ O-烷基化剂的比例为每摩尔O-烷基化剂0.5至1.5摩尔碱,O-烷基化剂/羟基苯酚的比例为0.5-2摩尔的O-烷基化剂/ 摩尔的羟基苯酚,有机溶剂/羟基苯酚的比例小于280mL,优选为10至250mL,更优选为50至150mL有机溶剂/摩尔羟基苯酚。 本发明还涉及从至少一种羟基苯酚化合物制备至少一种烷氧基 - 羟基苯甲醛的方法。
    • 9. 发明授权
    • Biodiesel purification by a continuous regenerable adsorbent process
    • 生物柴油通过连续可再生的吸附剂过程进行纯化
    • US08097049B2
    • 2012-01-17
    • US12366203
    • 2009-02-05
    • James R. MunsonBrian S. CookeBryan L. Bertram
    • James R. MunsonBrian S. CookeBryan L. Bertram
    • C10L1/19B01J49/00C07C45/54
    • B01D15/00B01D15/361B01J20/10B01J20/12B01J20/3433B01J20/3475B01J39/04B01J41/04B01J49/05B01J2220/58C07C67/56C10G2300/1014C10G2300/205C10G2300/4081C10G2300/44C10L1/026Y02E50/13Y02P30/20C07C69/52C07C69/24B01D15/265
    • A quick, economical and environmentally friendly, “green”, process for the continuous purification of biodiesel (fatty acid alkyl esters (FAAE)) is described using a powdered, granulated or extruded adsorbent. The adsorbent is contained in a column system and is regenerated for reuse multiple times. The process employs an adsorbent such as, but not limited to, carbon, silica, clay, zeolite or a metal silicate contained in a column to remove the impurities from fatty acid alkyl esters (FAAE) or crude biodiesel in a continuous process. The process utilizes the adsorbent column system for the purification of biodiesel, rather than water or filtration, to remove soaps and other impurities entrained in a crude biodiesel. The crude biodiesel is contacted with an adsorbent packed into a column, or multiple columns in series, for a sufficient amount of time to remove impurities such as, but not limited to, soaps, metals, free glycerin, sterol glucosides and many of the other impurities that reduce the stability of biodiesel. The resulting finished biodiesel exiting the column(s) is ready for the methanol recovery process. Once the adsorbent no longer removes the desired amount of impurities, it is regenerated for reuse. The solvent used for the regeneration process is reclaimed and reused by recycling it back to the transesterification reaction.
    • 使用粉末状,造粒或挤出的吸附剂描述了生物柴油(脂肪酸烷基酯(FAAE))的连续净化的快速,经济且环保的“绿色”方法。 吸附剂被包含在柱系统中并且被再生用于多次再利用。 该方法使用吸附剂,例如但不限于在柱中含有的碳,二氧化硅,粘土,沸石或金属硅酸盐,以在连续方法中除去脂肪酸烷基酯(FAAE)或粗生物柴油中的杂质。 该方法利用吸附柱系统来净化生物柴油,而不是水或过滤,以除去夹带在粗生物柴油中的肥皂和其他杂质。 将粗生物柴油与填充到柱中的吸附剂或多个串联的吸附剂接触足够的时间以除去杂质,例如但不限于皂,金属,游离甘油,固醇葡糖苷和许多其它的 降低生物柴油稳定性的杂质。 离开柱的结果最终的生物柴油可用于甲醇回收过程。 一旦吸附剂不再除去所需量的杂质,就可再生再生。 用于再生过程的溶剂通过回收到酯交换反应被回收再利用。