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| 1 | 甘油连续生物歧化过程的过渡行为及其数学模拟显示文摘用肺炎杆菌将甘油转化为1,3-丙二醇过程对稀释速率和底物进料浓度变化的过渡行为反映了细胞生长和胞内物质代谢在不同条件下存在着显著的差异。体系的过渡响应取决于操作条件变化前后系统所处的状态,当底物浓度由限制状态向剩余状态过渡时,甘油的残余浓度不断上升,而乙醇的浓度则逐渐下降,同时生物量、1,3-丙二醇和乙酸的浓度呈现先增后降的趋势。本文用“甘油浓度变化速率”的概念修正了菌体生长模型,并对甘油歧化过程的过渡响应进行了较好地描述。 | 修志龙 安利佳 曾安平 Deckwer Wolf-Dieter | 2000 | 高校化学工程学报2000，14，1： | 9 |
| 2 | 面包酵母细胞循环模型的实验验证显示文摘本文对作者早期提出的面包酵母细胞循环模型CCM进行了改进和动态实验验证。结果表明,CCM的动态特性基本与真实过程相符。基于该模型设计的酵母流加发酵最优进料控制策略的实施结果证实,CCM能够用于酵母生产的质量控制。 | 袁景淇 蒋慰孙 Bellgardt K.H. Deckwer W.D. | 1993 | 生物工程学报1993，9，1： | 2 |
| 3 | High concentration and productivity of 1,3-propanediol from continuous fermentation of glycerol by Klebsiella pneumoniae显示文摘 | Menzel K Zeng A P Deckwer W D | 1997 | Enzyme Microbiol Techol1997，，20： | 1 |
| 4 | Katalytische suspensionsreacktoren显示文摘 | Deckwer W D Alper E | 1980 | Chem Eng Tech1980，52，3： | 1 |
| 5 | Production and secretion of recombinant Leuconostoc mesenteroides dextransucrase DsrS in Bacillus megaterium显示文摘 | Marco Malten Rajan Hollmann Wolf-Dieter Deckwer | 2004 | Biotechnology and Bioengineering2004，89，2： | 1 |
| 6 | A kinetic model forsub strate and energy consumption of microbial growth under substrate - sufficient conditions 显示文摘 | ZENG A P DECKWER W D | 1995 | Biotechnol Prog1995，11，： | 1 |
| 7 | Stoichiometry, kinetics,and regulation of glucose and amino acid metubolism of a recombinant BHK cell line in batch and continous cultures显示文摘 | Linz M Zeng A.P Wagner R Deckwer W.D | | 0，，04： | 1 |
| 8 | Production of 2,3-butanediol in a membrane bioreactor with cell recycle 显示文摘 | Zeng A P Biebl H Deckwer W D | 1991 | Applied Microbiology and Biotechnology1991，34，4： | 1 |
| 9 | High concentration and of 1,3-propanediol from continuous fermentation of Klebsiella pneumoniae显示文摘 | Menzel K productivity glycerol by Technology Zeng A P Deckwer W D | 1997 | Enzyme and Microbial1997，20，2： | 1 |
| 10 | High concentration and productivity of 1,3-propanediol from continuous fermentation of glycerol by Klebsiella pneumoniae显示文摘 | MENZEL K ZENG A P DECKWER W D | 1997 | Enzyme Microbiol Technol1997，20，： | 1 |
| 11 | High concentration and productivity of 1,3-propanediol from continuous fermentation of glycerol by Klebsiella pneumoniae显示文摘 | Menzel K Zeng A P Deckwer W D | 1997 | Enzyme Microb Technol1997，，20： | 1 |
| 12 | Modeling the Fischer-Tropsch synthesis in the slurry phase显示文摘 | DECKWER W D SERPEMEN Y RALEK M | 1982 | Industrial & Engineering Chemistry Process Design and Development1982，21，2： | 1 |
| 13 | Biodegradation of polyesters containing aromatic constituents显示文摘 | MULLER R KLEEBERG I Deckwer W | 2001 | Journal of Biotechnology2001，86，2： | 1 |
| 14 | Production of 2,3-butanediol in a membrane bioreactor with cell recycle 显示文摘 | Biebl H Deckwer WD | 1991 | Appl Microbiol Biotechnol1991，34，： | 1 |
| 15 | 显示文摘 | Uwe Witt Rol-Joaehim Maller Wolf Dieter Deckwer | 1996 | Macrornol Chem Phys1996，197，： | 1 |
| 16 | Bacterial alginate: physiology, product quality and process aspects显示文摘 | W. Sabra A.-P. Zeng W.-D. Deckwer | 2001 | Applied Microbiology and Biotechnology (-)2001，，3： | 1 |
| 17 | Gas absorption mechanism in catalytic slurry reactors 显示文摘 | ALPER WICHTENDAHL B DECKWER W D | 1980 | Chem Eng Sci1980，35，： | 1 |
| 18 | Einsatz der adsorption zur produtsabtrennung bei der glycerinvergarung zu 1,3-propanediol显示文摘 | Schlieker H Gunzel B Deckwer W D | 1992 | Chem Ing Tech1992，64，8： | 1 |
| 19 | Production of 1,3-propanediol by Clostridium butyricum in ontinuous culture with cell recycling显示文摘 | Reimann A Biebl H Deckwer W D | 1998 | Appl Microbiol Biotechnol1998，，49： | 1 |
| 20 | Organic liquids in a bubble column:Hold up and mass transfer coefficients显示文摘 | Ozturk S S Schumpe A Deckwer W D | 1987 | AIChE J1987，33，10： | 1 |
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