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1. 发明申请

WO2007135188A2 PROCESS FOR THE PREPARATION OF L-METHIONINE 审中-公开
标题翻译：制备L-甲硫氨酸的方法
公开(公告)号：WO2007135188A2
公开(公告)日：2007-11-29
申请号：PCT/EP2007055056
申请日：2007-05-24
申请人： BASF AG , ZELDER OSKAR , HEROLD ANDREA , KLOPPROGGE CORINNA , SCHROEDER HARTWIG , HEINZLE ELMAR , WITTMANN CHRISTOPH , KROEMER JENS , PERO JANICE , YOCUM ROGERS , PATTERSON THOMAS , WILLIAMS MARK , HERMANN THERON
发明人： ZELDER OSKAR , HEROLD ANDREA , KLOPPROGGE CORINNA , SCHROEDER HARTWIG , HEINZLE ELMAR , WITTMANN CHRISTOPH , KROEMER JENS , PERO JANICE , YOCUM ROGERS , PATTERSON THOMAS , WILLIAMS MARK , HERMANN THERON
IPC分类号： C12P13/12
CPC分类号： C12P13/12
摘要： The present invention relates to microorganisms and processes for the efficient preparation of L-methionine. In particular, the present invention relates to processes in which the amount of serine available for the metabolism of the microorganism is increased.
摘要翻译：本发明涉及用于L-甲硫氨酸有效制备的微生物和方法。特别地，本发明涉及其中可用于微生物代谢的丝氨酸量增加的方法。

2. 发明申请

WO2007020295A3 MICROORGANISMS WITH INCREASED EFFICIENCY FOR METHIONINE SYNTHESIS 审中-公开
标题翻译： MICROORGANISMS对提高蛋氨酸合成的效率
公开(公告)号：WO2007020295A3
公开(公告)日：2007-05-03
申请号：PCT/EP2006065460
申请日：2006-08-18
申请人： BASF AG , ZELDER OSKAR , HEROLD ANDREA , KLOPPROGGE CORINNA , SCHROEDER HARTWIG , HAEFNER STEFAN , HEINZLE ELMAR , WITTMANN CHRISTOPH , KROEMER JENS , PERO JANICE , YOCUM ROGERS , PATTERSON THOMAS , WILLIAMS MARK , HERMAN THERON
发明人： ZELDER OSKAR , HEROLD ANDREA , KLOPPROGGE CORINNA , SCHROEDER HARTWIG , HAEFNER STEFAN , HEINZLE ELMAR , WITTMANN CHRISTOPH , KROEMER JENS , PERO JANICE , YOCUM ROGERS , PATTERSON THOMAS , WILLIAMS MARK , HERMAN THERON
IPC分类号： C12N15/52 , C12P13/12 , C12R1/13 , C12R1/19
CPC分类号： C12N15/52 , C12P13/12
摘要： The present invention concerns methods for the production of microorganisms with increased efficiency for methionine synthesis. The present invention also concerns microorganisms with increased efficiency for methionine synthesis. Furthermore, the present invention concerns methods for determining the optimal metabolic flux for organisms with respect to methionine synthesis.
摘要翻译：本发明涉及生产甲硫氨酸合成效率提高的微生物的方法。本发明还涉及甲硫氨酸合成效率提高的微生物。此外，本发明涉及用于确定与甲硫氨酸合成有关的生物体的最佳代谢通量的方法。

3. 发明申请

WO2007051725A3 MICROORGANISM AND PROCESS FOR THE PREPARATION OF L-METHIONINE 审中-公开
标题翻译：用于制备L-甲硫氨酸的微生物和方法
公开(公告)号：WO2007051725A3
公开(公告)日：2007-06-28
申请号：PCT/EP2006067680
申请日：2006-10-23
申请人： BASF AG , ZELDER OSKAR , HEROLD ANDREA , KLOPPROGGE CORINNA , SCHROEDER HARTWIG , HAEFNER STEFAN , HEINZLE ELMAR , WITTMANN CHRISTOPH , KROEMER JENS , PERO JANICE G , YOCUM R ROGERS , PATTERSON THOMAS A , WILLIAMS MARK , HERMAN THERON
发明人： ZELDER OSKAR , HEROLD ANDREA , KLOPPROGGE CORINNA , SCHROEDER HARTWIG , HAEFNER STEFAN , HEINZLE ELMAR , WITTMANN CHRISTOPH , KROEMER JENS , PERO JANICE G , YOCUM R ROGERS , PATTERSON THOMAS A , WILLIAMS MARK , HERMAN THERON
IPC分类号： A23K1/00 , C12N15/52 , C12P13/12
CPC分类号： C12P13/12 , A23K10/16 , A23K20/142 , A23K40/10 , C12N15/52
摘要： The present invention relates to microorganisms and processes for the efficient preparation of L-amino acids such as L-methionine. In particular, the present invention relates to microorganisms and processes in which the formation and/or accumulation of homolanthionine in the methionine pathway is reduced and/or prevented.
摘要翻译：本发明涉及用于有效制备L-氨基酸如L-甲硫氨酸的微生物和方法。特别地，本发明涉及微生物和其中甲硫氨酸途径中高山ion素的形成和/或积累减少和/或预防的方法。

4. 发明申请

WO0243863A3 FRACTIONAL REGENERATION OF A WEAKLY ACIDIC ION EXCHANGER LOADED WITH BIVALENT METALLIC IONS 审中-公开
标题翻译：与二价金属离子分数再生LOADED弱酸性离子交换
公开(公告)号：WO0243863A3
公开(公告)日：2003-05-01
申请号：PCT/EP0112972
申请日：2001-11-09
申请人： HENKEL KGAA , LEPA KLAUS , KROEMER JENS , DRONIOU PATRICK , BROUWER JAN-WILLEM , KUHM PETER , MAUER DIETER
发明人： LEPA KLAUS , KROEMER JENS , DRONIOU PATRICK , BROUWER JAN-WILLEM , KUHM PETER , MAUER DIETER
IPC分类号： B01J49/00 , C23C22/86
CPC分类号： C23C22/86 , B01J49/53
摘要： The invention relates to a method for the fractional regeneration of a weakly acidic ion exchanger loaded with bivalent metallic ions selected from nickel, zinc and manganese ions, obtaining a phosphoric acid solution of valuable substances, containing said metallic ions. At least two portions of aqueous phosphoric acid are successively loaded onto the ion exchanger, each successive portion of aqueous phosphoric acid having a weaker concentration of phosphoric acid than the precedent. After loading the first portion of aqueous phosphoric acid onto the ion exchanger in the form of a phosphoric acid solution of valuable substances containing metallic ions, a fraction of the concentrate is discharged. Said fraction contains at least 0.5 wt. % of metallic ions and the volume thereof is no larger than double the volume of the first portion of aqueous phosphoric acid. Further fractions of the regenerated product are collected, the respective volumes thereof not differing by more than 50 % of the volumes of the portions of aqueous phosphoric acid loaded onto the ion exchanger in order to produce the respective fractions of the regenerated product. After the last portion of aqueous phosphoric acid is loaded, a rewashing is carried out with enough water to drive the last portion of aqueous phosphoric acid from the ion exchanger and collect it as a last fraction of the regenerated product. Either so much phosphoric acid having a concentration of between 60 and 95 wt. % is deposited on the ion exchanger that the loss of phosphoric acid of the first fraction of the regenerated product is compensated for in relation to the first loaded portion of aqueous phosphoric acid and, for the next regeneration cycle, the fractions of the regenerated product which are obtained in the preceding cycle are loaded in the form of portions of aqueous phosphoric acid in the order obtained, or, the first fraction of the regenerated product collected following the discharge of the fraction of concentrate is mixed with such a quantity of concentrated phosphoric acid that the phosphoric acid concentration in said fraction of the regenerated product and the volume of said fraction of regenerated product correspond essentially to the phosphoric acid concentration and the volume of the original first portion of aqueous phosphoric acid before being loaded onto the ion exchanger. For a corresponding succeeding regeneration cycle of a weakly acidic ion exchanger loaded with the appropriate metallic ions, the individual fractions of the regenerated product from the preceding regeneration cycle are loaded onto the ion exchanger, in the order obtained, in the form of individual portions of aqueous phosphoric acid.
摘要翻译：与选自镍，锌和锰离子的分数再生选择的二价金属离子的方法加载的弱酸性离子交换剂，得到磷酸，含有这些金属离子有价值的产品的解决方案，其中，一个连续的离子交换放弃磷酸水溶液，其中每个相继的块中的至少两个部分具有较低的酸浓度比前一个，磷酸水溶液，其中一个ausschleust磷酸水溶液的第一部分应用到比离子交换后浓缩液级分的磷酸金属含有至少0.5贵重材料的溶液。含有金属离子和它们的体积的％含离子不大于磷酸水溶液的所述第一部分的两倍体积越大，则进一步再生级分通过没有相应的生成雷杰的体积的50％以上，其字段各自的体积不同装填到磷酸水溶液的离子交换部分Nerat馏分，nachwäscht与至少这么多的水使最终部分从离子交换器置换的磷酸水溶液，并收集作为最后的再生部分，无论是在离子交换放弃磷酸水溶液的最后部分之后，从而具有在60％至95％（重量）的范围内的浓度多磷酸应用于的第一再生馏分相对于所述第一不连续部的磷酸水溶液的磷酸 - 损失被补偿，然后用于下一个再生循环中，再生在前面的周期中获得所获得的序列中的级分给出的磷酸水溶液，或排出浓缩液级分收集再生馏分浓磷酸的这样的量混合后的第一个的部分，即两个Konzentra 磷酸在再生馏分和再生部分的体积大致磷酸浓度和含水磷酸当量的离子交换剂装载的原始第一部分的体积，和一个用于的与适当的对应的随后的再生循环的灰金属离子从所获得的序列中的前面的再生循环加载弱酸性离子交换剂再生的各个级分给出的磷酸水溶液的离子交换剂的各个部分。

5. 发明申请

WO2004063424A3 TWO-STAGE OR MULTI-STAGE METHOD FOR TREATING PHOSPHATED RINSING WATER USING A MEMBRANE 审中-公开
标题翻译：磷灰石废水的两次或多次膜处理
公开(公告)号：WO2004063424A3
公开(公告)日：2004-12-02
申请号：PCT/EP0313392
申请日：2003-11-28
申请人： HENKEL KGAA , DRONIOU PATRICK , KROEMER JENS , LEPA KLAUS , BROUWER JAN-WILLEM , PEIROW IRADJ , KUHM PETER
发明人： DRONIOU PATRICK , KROEMER JENS , LEPA KLAUS , BROUWER JAN-WILLEM , PEIROW IRADJ , KUHM PETER
IPC分类号： B01D61/02 , C02F1/44 , C23C22/86 , C23C22/00
CPC分类号： C23C22/86 , B01D61/022 , C02F1/44 , C02F1/441 , C02F2103/16
摘要： The invention relates to a method for phosphating metallic surfaces. According to said method, the metallic surfaces are rinsed with rinsing water after phosphation, and the rinsing water is subjected to a two-stage or multi-stage nanofiltration process. The concentrate of a nanofiltration stage is respectively used as a parent solution for the ensuing nanofiltration stage. The concentrate of the last nanofiltration stage is used to complete the phosphation solution.
摘要翻译：一种磷化金属表面的方法，其中金属表面在磷化后用漂洗水冲洗并且冲洗水经过两阶段或多阶段纳滤。在每种情况下，纳滤阶段的浓缩物都可用作后续纳滤阶段的起始溶液。最后的纳滤阶段的浓缩物用于补充磷化溶液。

6. 发明申请

WO0240405A3 TREATMENT OF NICKEL-CONTAINING WASTE WATER ON PHOSPHATING 审中-公开
标题翻译：污水中的镍 - 磷酸盐化处理
公开(公告)号：WO0240405A3
公开(公告)日：2002-07-25
申请号：PCT/EP0112814
申请日：2001-11-06
申请人： HENKEL KGAA , LEPA KLAUS , KROEMER JENS , DRONIOU PATRICK , BROUWER JAN-WILLEM , KUHM PETER
发明人： LEPA KLAUS , KROEMER JENS , DRONIOU PATRICK , BROUWER JAN-WILLEM , KUHM PETER
IPC分类号： B01D61/02 , B01D61/14 , B01J39/04 , B01J45/00 , B01J49/00 , C02F1/42 , C23C22/22 , C23C22/86 , B01J39/00
CPC分类号： C23C22/86 , B01J39/07 , B01J45/00 , C02F1/42
摘要： Method for the treatment of a nickel-containing waste water, comprising a phosphate bath overflow and/or the rinsing water after phosphating, whereby the phosphating is carried out with an acidic aqueous phosphate solution, containing 3 to 50 g/l phosphate ions, calculated as PO4-3, 0.2 to 3 g/l zinc ions, 0.01 to 2.5 g/l nickel ions, optionally further metal ions and optionally accelerator. The phosphate bath overflow and/or post-phosphating rinsing water are run over a weakly acidic ion-exchanger, characterised in that the acid groups of the ion exchanger are neutralised with alkali metal ions to no more than 15 % and that on supplying the nickel-containing aqueous solution to the ion exchanger said solution has a pH value in the range 2.5 to 6.0.
摘要翻译：一种用于治疗由磷化和/或磷化后漂洗水含镍的水溶液处理，磷化用的酸性水溶液的磷化溶液，其计算为3至50g / l的磷酸根离子，作为PO4-3进行，0.2到3g 包含/升的锌离子，0.01至2.5g /镍离子，任选地另外的金属离子和任选的促进剂的升，由此磷化和/或漂洗水被磷化通过弱酸性离子交换后进行的，其特征在于，所述酸基团离子交换剂被中和至不超过15％的碱金属离子和含镍水溶液中，同时将在离子交换剂具有的pH范围为2.5至6.0有。

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