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    • 2. 发明申请
    • FERMENTATION PROCESS AT REDUCED PRESSURE
    • 降低压力的发酵过程
    • WO2011045365A1
    • 2011-04-21
    • PCT/EP2010/065395
    • 2010-10-14
    • PURAC BIOCHEM BVVAN BREUGEL, JanGROOT, Willem JacobJANSEN, Peter Paul
    • VAN BREUGEL, JanGROOT, Willem JacobJANSEN, Peter Paul
    • C12P1/00C12P7/46C12P7/56
    • C12P1/00C12P7/46C12P7/56
    • The present invention pertains to a fermentation process wherein a carbohydrate source is contacted under fermentation conditions with a microorganism in an aqueous fermentation broth to form a fermentation product which is a salt or a product with a boiling point above the boiling point of water, wherein the fermentation process is carried out aτ; a pressure which is below atmospheric pressure and at least at the value where the reaction medium is at its boiling point at the fermentation temperature, with water being evaporated and removed from the reactor during the fermentation in an amount which is at least 20% of the volume of liquid present in the reactor at the start of the fermentation. It has been found that effecting a fermentation process at reduced pressure while removing a substantial amount of water has a number of advantages. It solves the problem of having a surplus of water in the system, it ensures removal of reaction heat, and may lead to improved fermentation quality.
    • 本发明涉及一种发酵方法,其中碳水化合物源在发酵条件下与含水发酵液中的微生物接触以形成发酵产物,其为沸点高于水沸点的盐或产物,其中 发酵过程在 压力低于大气压,至少在反应介质处于发酵温度沸点的温度下,在发酵期间蒸发和从反应器中除去水的量至少为发酵温度的20% 在发酵开始时反应器中存在的液体体积。 已经发现,在减少大量水的同时在减压下进行发酵过程具有许多优点。 解决了系统中多余的水分问题,确保了反应热的去除,可以提高发酵品质。
    • 6. 发明公开
    • PROCESS FOR THE CONTINUOUS PRODUCTION OF POLYESTERS
    • VERFAHREN ZUR KONTINUIERLICHEN HERSTELLUNG VON POLYESTERN
    • EP2310437A1
    • 2011-04-20
    • EP09781236.6
    • 2009-07-29
    • PURAC Biochem BVSulzer Chemtech AG
    • HAAN, Robert EdgarJANSEN, Peter PaulDE VOS, Siebe CornelisVAN BREUGEL, JanKREIS, Peter WilliLANFRANCHI, Sarah
    • C08G63/78
    • C08G63/785C08G63/08
    • Continuous process of forming aliphatic polyesters The process includes continuously providing cyclic ester monomer and polymerization catalyst to a continuous mixing loop reactor (CMLR) having static mixing elements and operated at a temperature between 100 and 240° C. to form a pre-polymerized reaction mixture. The conversion is between 40 and less than 90 wt. %, wherein the cyclic ester monomer comprises lactide having a free acid content lower than 50 milli-equivalents per kg. The pre-polymerized reaction mixture is continuously provided to a plug flow reactor that is a static mixer reactor having static mixing elements and is operated at a temperature between 110-240° C., wherein the reaction mixture is polymerized to a conversion of at least 90%, to form polymer wherein the flow ratio of the CMLR and the plug flow reactor is between 1.5 an d50. The process includes continuously removing polymer from the plug flow reactor devolitizing the polymer.
    • 在100-240℃的温度下环状酯单体开环聚合以形成脂族聚酯的连续方法,其包括a)连续地向连续混合反应器提供环状酯单体和聚合催化剂,反应器在 有效聚合以形成预聚合的反应混合物的条件,b)从连续混合反应器中连续除去预聚合的反应混合物,并将连续提供预聚合的反应混合物连续提供给活塞流反应器,活塞流反应器在聚合条件下操作 其中反应混合物聚合至至少90%的聚合度,以形成聚合物,和c)从活塞流反应器中连续除去聚合物。