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    • 2. 发明授权
    • Process for obtaining 2-hydroxy-4-methylthiobutyric acid (MHA)
    • 获得2-羟基-4-甲硫基丁酸(MHA)的方法
    • US6140536A
    • 2000-10-31
    • US91796
    • 1998-09-01
    • Hans Albrecht HassebergHans Joachim HasselbachKlaus HuthmacherVolker HafnerHarald HeinzelBarbara Jager
    • Hans Albrecht HassebergHans Joachim HasselbachKlaus HuthmacherVolker HafnerHarald HeinzelBarbara Jager
    • C07C319/20C07C319/28C07C323/52C07C315/00
    • C07C319/28C07C319/20
    • A method for the isolation of 2-hydroxy-4-methylthiobutyric acid (MHA), wherein MHA is isolated from a reaction mixture obtained by addition of hydrogen cyanide (HCN) to methylmercaptopropionaldehyde (MMP) and hydrolysis by sulphuric acid of the methylmercaptopropionaldehyde cyanohydrin (MMP-CH) thus obtained. The reaction mixture is brought into contact in a liquid/liquid extraction system with an organic solvent substantially immiscible with water, in order to form an extraction solution which contains the solvent and the MHA transferred out of the reaction mixture. By bringing the salt content of the reaction mixture, prior to the liquid/liquid extraction, to a concentration of about >50 wt. % (wt./wt.), preferably >55 wt. %, referred to the sum of the inorganic constituents of the reaction mixture, the coordinated use of energy in the total system is improved, the evaporation of strongly corrosive solutions is avoided, the efficiency of the hydrolysis step is increased and the distribution coefficients during the extraction are improved. The MHA is isolated as the extract from this extraction solution by evaporation, and may be used as animal feed supplement.
    • PCT No.PCT / EP96 / 05437 Sec。 371日期:1998年9月1日 102(e)1998年9月1日PCT PCT 1996年12月5日PCT公布。 公开号WO97 / 23452 日期1997年7月3日分离2-羟基-4-甲硫基丁酸(MHA)的方法,其中MHA是通过将氰化氢(HCN)加入到甲基巯基丙醛(MMP)中并通过硫酸水解而获得的反应混合物中分离的 的甲基巯基丙醛氰醇(MMP-CH)。 使反应混合物在液/液萃取系统中与基本上与水不混溶的有机溶剂接触,以形成含有溶剂和从反应混合物中转移的MHA的萃取溶液。 通过使液体/液体萃取之前的反应混合物的盐含量达到约> 50wt。 %(重量/重量),优选> 55重量% %,是指反应混合物的无机成分之和,改善了总体系中能量的协调使用,避免了强腐蚀性溶液的蒸发,提高了水解步骤的效率,提高了分散系数 提取提高。 通过蒸发将MHA作为来自该提取溶液的提取物分离,并且可以用作动物饲料添加剂。
    • 4. 发明授权
    • Process for recovering 2-hydroxy-4-methylthiobutyric acid (MHA), MHA and
its use
    • 2-羟基-4-甲硫基丁酸(MHA),MHA及其用途的回收方法
    • US5976609A
    • 1999-11-02
    • US776217
    • 1997-01-13
    • Hans-Albrecht HassebergKlaus HuthmacherHerbert TannerVolker HafnerHarald Heinzel
    • Hans-Albrecht HassebergKlaus HuthmacherHerbert TannerVolker HafnerHarald Heinzel
    • A23K1/16C07C319/20C07C319/28C07C323/52C07C323/60A23L1/305A23L1/28C15C315/02C15C315/06
    • C07C319/28A23K20/105C07C319/20Y10S426/807
    • It is known to isolate MHA from a reaction mixture obtained by the addition of hydrocyanic acid (HCN) to methyl mercaptopropionic aldehyde (MMP) and the hydrolysis of the methyl mercapto propionic aldehyde cyanohydrine (MMP-CH) obtained thereby with sulphuric acid, in which the reaction mixture is brought into contact with a substantially non-water-miscible organic solvent, in order to form an extraction solution having the solvent and MHA transferred from the reaction mixture, and the MHA is obtained as an extract from this extraction solution by concentration. The simplest and most economical process of the invention concerning the processing of the reaction product which facilitates the production of a highly concentrated product with an extremely low dimer, oligomer and by-product content, is characterised in that the concentration is conducted in such a way that the remaining extract contains less than 4 wt % and preferably less than 2 wt % of water. Animal feed supplement, mixtures for supplementing animal feed, e.g. with methionine or ammonium-MHA.
    • PCT No.PCT / EP95 / 02515 Sec。 371日期1997年1月13日 102(e)日期1997年1月13日PCT提交1995年6月28日PCT公布。 公开号WO96 / 01809 日本1996年1月25日已知通过将氢氰酸(HCN)加入到甲基巯基丙醛(MMP)中获得的反应混合物和由此获得的甲基巯基丙醛氰基氢醌(MMP-CH)的水解来分离MHA 硫酸,其中使反应混合物与基本上不与水混溶的有机溶剂接触,以形成从反应混合物中转移有溶剂和MHA的提取溶液,并且获得MHA作为 该提取液通过浓缩。 关于有助于生产具有极低二聚体,低聚物和副产物含量的高浓缩产物的反应产物的加工的本发明的最简单和最经济的方法的特征在于以这种方式进行浓缩 剩余的提取物含有小于4重量%,优选小于2重量%的水。 动物饲料补充剂,补充动物饲料的混合物。 与甲硫氨酸或铵-MAA。
    • 7. 发明授权
    • Process for producing 2-hydroxy-4-methylthiobutyric acid (MHA) and its
use as feed stuff supplement
    • 制备2-羟基-4-甲硫基丁酸(MHA)的方法及其作为饲料添加剂的使用
    • US5847207A
    • 1998-12-08
    • US793113
    • 1997-05-13
    • Helmut SuchslandVolker Hafner
    • Helmut SuchslandVolker Hafner
    • A23K1/16C07C319/20C07C319/28C07C323/52C07C323/60C07C315/00
    • C07C319/20C07C319/28
    • Known processes for producing 2-hydroxy-4-methylthiobutyric acid (MHA) use a liquid-liquid extraction or a combined liquid/liquid and solid/liquid phase separation to isolate MHA from a reaction mixture produced by hydrolysing MMP-cyanhydrine. These processes are either costly or produce waste that is difficult to dispose of. These disadvantages are eliminated by isolating MHA by solid/liquid separation. The reaction mixture is evaporated until a MHA-containing salt residue with little or no residual water is obtained the MHA-containing, salt residue is treated with an organic solvent to produce a suspension, solid components are separated from the thus obtained suspension until a MHA-containing solution is obtained, the organic solvent is removed from the MHA-containing solution until a MHA residue is obtained and if required the MHA residue is then conditioned by water admixture. Besides high quality MHA, this process produces marketable crystalline ammonium sulphate and/or hydrogenated ammonium sulphate. This process is useful for producing feedstuff supplements.
    • PCT No.PCT / EP95 / 03068 Sec。 371日期1997年5月13日 102(e)日期1997年5月13日PCT提交1995年8月2日PCT公布。 公开号WO96 / 05173 日期1996年2月22日生产2-羟基-4-甲硫基丁酸(MHA)的方法采用液 - 液萃取或液 - 液和液/液相组合分离,从通过水解MMP- 氰水。 这些过程是昂贵的或产生难以处置的废物。 通过固/液分离隔离MHA来消除这些缺点。 将反应混合物蒸发直到得到具有少量或不残留水的含MHA的盐残余物,含有MHA的盐残余物用有机溶剂处理以产生悬浮液,将固体组分从如此获得的悬浮液中分离直到MHA 得到的有机溶剂从含有MHA的溶液中除去,直到获得MHA残留物,如果需要,则通过水混合物对MHA残余物进行调理。 除了高品质的MHA之外,该方法还生产了市售的结晶硫酸铵和/或氢化的硫酸铵。 此过程对生产饲料添加剂有用。
    • 9. 发明申请
    • Vacuum drainage system
    • 真空排水系统
    • US20050072468A1
    • 2005-04-07
    • US10679742
    • 2003-10-06
    • Volker HafnerThomas ZinnEnrique Loreto
    • Volker HafnerThomas ZinnEnrique Loreto
    • E03F1/00F04F3/00
    • E03F1/006Y10T137/0379Y10T137/3109
    • A vacuum drainage system operable to remove waste from a source. The system includes an accumulator in fluid communication with the source and a substantially vertical riser having a first portion in fluid communication with the accumulator and a second portion downstream of the first portion and in fluid communication with a vacuum source. A first valve is disposed between the first portion and the second portion. The first valve is selectively operable to provide fluid communication between the first portion and the vacuum source. An air inlet is disposed a distance downstream of the first valve and is selectively operable to provide fluid communication between the outside atmosphere and the second portion.
    • 真空排水系统可操作以从源中除去废物。 该系统包括与源流体连通的蓄能器和具有与蓄能器流体连通的第一部分和第一部分下游的第二部分并与真空源流体连通的基本垂直的提升管。 第一阀设置在第一部分和第二部分之间。 第一阀选择性地可操作以在第一部分和真空源之间提供流体连通。 空气入口设置在第一阀下游的距离处,并且可选择性地操作以在外部气氛和第二部分之间提供流体连通。