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    • 4. 发明授权
    • High-yield production of organic nitriles
    • 高产量生产有机腈
    • US08471052B2
    • 2013-06-25
    • US12622782
    • 2009-11-20
    • Anil OroskarPaul Roman KurekAsha Oroskar
    • Anil OroskarPaul Roman KurekAsha Oroskar
    • C07C253/00
    • C07C253/00C01C3/0204C07C253/34C07C255/03
    • A process is disclosed for producing organic nitriles such as Acetonitrile or Hydrogen Cyanide, in which yields may exceed 90%, undesirable by-products are not produced, and handling of ammonia gas is avoided. In one aspect, a process includes preparing a feed including ammonium salts and water; introducing the feed into a reactor containing a catalyst; and heating the feed in the presence of the catalyst. The catalyst may advantageously include molybdenum on a silica or silica alumina support. The feed may be ammonium acetate in water with about 50 wt % ammonium acetate and the balance water or ammonium formate in water. In another aspect, a process includes preparing a feed including ammonium hydroxide and acetic acid; introducing the feed into a reactor containing a catalyst; and heating the feed in the presence of the catalyst.
    • 公开了用于生产有机腈如乙腈或氰化氢的方法,其中产率可能超过90%,不会产生不期望的副产物,并且避免了氨气的处理。 一方面,一种方法包括制备包括铵盐和水的进料; 将进料引入含有催化剂的反应器中; 并在催化剂存在下加热进料。 催化剂可以有利地包括二氧化硅或二氧化硅氧化铝载体上的钼。 进料可以是水中的乙酸铵与约50重量%的乙酸铵和余量的水或甲酸铵的水溶液。 另一方面,一种方法包括制备包含氢氧化铵和乙酸的进料; 将进料引入含有催化剂的反应器中; 并在催化剂存在下加热进料。
    • 9. 发明申请
    • SMB Process For Producing Highly Pure EPA From Fish Oil
    • 用于从鱼油生产高纯度EPA的SMB方法
    • US20150166929A1
    • 2015-06-18
    • US13880146
    • 2012-07-06
    • Adam KelliherAngus MorrisonAnil OroskarRakesh Vikraman Nair RemaAbhilesh Agarwal
    • Adam KelliherAngus MorrisonAnil OroskarRakesh Vikraman Nair RemaAbhilesh Agarwal
    • C11B3/00B01D15/18
    • C11B3/00B01D15/185B01D15/1892C11C1/005C11C1/08
    • The present invention provides a chromatographic separation process for recovering a polyunsaturated fatty acid (PUFA) product from a feed mixture which is a fish oil or which is derived from fish oil, which process comprises the steps of: (i) purifying the feed mixture in a chromatographic separation step, to obtain a first intermediate product; and (ii) purifying the first intermediate product obtained in (i) in a simulated or actual moving bed chromatographic separation step, to obtain a second intermediate product; and (iii) purifying the second intermediate product obtained in (ii) in a simulated or actual moving bed chromatographic separation step, to obtain the PUFA product; wherein an aqueous organic solvent is used as eluent in each separation step; saturated and/or monounsaturated fatty acids present in the feed mixture are removed in the first separation step; the PUFA product is separated from different components of the feed mixture in steps (ii) and (iii); and the PUFA product obtained in the third separation step contains EPA or an EPA derivative in an amount greater than 90 wt %.
    • 本发明提供了一种色谱分离方法,用于从作为鱼油的饲料混合物或鱼油中回收多不饱和脂肪酸(PUFA)产物,该方法包括以下步骤:(i)将进料混合物纯化 色谱分离步骤,以获得第一中间产物; 和(ii)在模拟或实际移动床色谱分离步骤中纯化(i)中获得的第一中间产物,以获得第二中间产物; 和(iii)在模拟或实际移动床层析分离步骤中纯化(ii)中得到的第二中间产物,得到PUFA产物; 其中在每个分离步骤中使用含水有机溶剂作为洗脱剂; 存在于进料混合物中的饱和和/或单不饱和脂肪酸在第一分离步骤中被除去; 在步骤(ii)和(iii)中将PUFA产物与进料混合物的不同组分分离; 并且在第三分离步骤中获得的PUFA产物含有大于90重量%的EPA或EPA衍生物。
    • 10. 发明申请
    • SMB Process
    • SMB流程
    • US20140200360A1
    • 2014-07-17
    • US13880154
    • 2012-07-06
    • Adam KelliherAngus MorrisonAnil OroskarRakesh Vikraman Nair RemaAbhilesh Agarwal
    • Adam KelliherAngus MorrisonAnil OroskarRakesh Vikraman Nair RemaAbhilesh Agarwal
    • C11C1/02
    • C11C1/02B01D15/185B01D15/1892C11B7/0008C11B7/0025C11C1/005C11C1/007
    • The present invention provides a chromatographic separation process for recovering a polyunsaturated fatty acid (PUFA) product from a feed mixture, which process comprises the steps of: (i) purifying the feed mixture in a first separation step in a simulated or actual moving bed chromatography apparatus having a plurality of linked chromatography columns containing, as eluent, an aqueous organic solvent, to obtain an intermediate product; and (ii) purifying the intermediate product obtained in (i) in a second separation step using a simulated or actual moving bed chromatography apparatus having a plurality of linked chromatography columns containing, as eluent, an aqueous organic solvent, to obtain the PUFA product; wherein (a) the first and second separation steps are carried out sequentially on the same chromatography apparatus, the intermediate product being recovered between the first and second separation steps and the process conditions in the chromatography apparatus being adjusted between the first and second separation steps such that the PUFA product is separated from different components of the feed mixture in each separation step; or (b) the first and second separation steps are carried out on separate first and second chromatography apparatuses respectively, the intermediate product obtained from the first separation step being introduced into the second chromatography apparatus, and the PUFA product being separated from different components of the feed mixture in each separation step.
    • 本发明提供了用于从进料混合物中回收多不饱和脂肪酸(PUFA)产物的色谱分离方法,该方法包括以下步骤:(i)在模拟或实际移动床层析中在第一分离步骤中纯化进料混合物 具有多个连接的色谱柱的装置,其包含含水有机溶剂作为洗脱剂,以获得中间产物; 和(ii)使用具有多个相连的色谱柱的模拟或实际移动床层析装置,在第二分离步骤中纯化在(i)中获得的中间产物,所述色谱柱含有水性有机溶剂作为洗脱液,得到PUFA产物; 其中(a)第一和第二分离步骤在相同的色谱装置上依次进行,中间产物在第一和第二分离步骤之间回收,色谱装置中的工艺条件在第一和第二分离步骤之间进行调整, 在每个分离步骤中将PUFA产物与进料混合物的不同组分分离; 或(b)第一和第二分离步骤分别在分离的第一和第二色谱装置上进行,将从第一分离步骤获得的中间产物引入第二色谱装置中,并将PUFA产物从 进料混合物。