The results showed that the corrected formula of Monod equation well described the rule of the degradation of butanediol.
结果表明Monod方程的修正式能很好地描述丁二醇的降解规律，试验温度下Monod方程的修正式为：v=0.044(S-100)/[5719 (S-100)]。
Through an analysis of experimental data, equations about organic matter degraded, anaerobic and phosphorus removal wholly accord with first class dynamics model.
通过对实验数据的分析，证明厌氧释磷和厌氧有机质降解方程均符合Monod一级动力学模型。
Systemly measures COD and VFA and pH and alkalinity of outflow and methane yield and temperature, calculates COD removal rate and cubage loading and hydraulic loading, studies the running rule of ABR and its chambers, for the first time discusses and analyse the phenomenon of acidification phase separating with methane phase and the mode of increase loading Reactor acidification and comeback are studied. Hydraulic characteristics is analysed by tracing experiment. The relationship of sludge quantity in ABR with running and sludge granulation is discussed by observation channel phenomenon and sludge granulation. Analysis of running parameter indicates that sludge loading can image generally the factor influencing reactor running, and for the first time edgeout substance concentration by sludge loading in monod model, and found a biology digestion kenetic model, at last calculate kenetic parameters using experimental date and make comparation between measure date and fore cast date.
系统地测量了出水中COD、VFA、pH、碱度及甲烷产量、温度等指标，计算了COD去除率、容积负荷、水力负荷等运行参数，研究了ABR反应器及各个格室的运行规律，并首次讨论和分析了ABR内产酸相与产甲烷相分离现象和ABR提高负荷的方式；研究了反应器酸化及恢复措施；通过示踪试验分析ABR的水力特性；通过观测ABR污泥床内沟流现象、颗粒污泥的形成、污泥颗粒化程度探讨了ABR内污泥量与反应器运行及污泥颗粒化的关系；对运行参数的分析表明污泥负荷能够全面的反映影响反应器运行的因素，首次以污泥负荷替代Monod模式中的基质浓度，建立了ABR的生物降解动力学模型，用取得的试验数据计算了动力学参数并比较实测值与预测值。
It is very easy to implement since the carbon dioxide excretion rate can be obtained easily.
另一种办法是把比生长率作为发酵液中基质浓度的函数，如Monod模型[1]。
When nitrite accumulation occurred temperately in the system, piecewise zero-order kinetic model and dynamic model based on Monod equations were both used to describe the experimental data, and related parameters were analyzed.
在系统亚硝酸盐暂时积累条件下，分别采用分段零级动力学模型和基于Monod方程的动态模型，拟合试验数据，并求算相应的动力学参数。
The experimental results showed that Monod equation can express the relationship between the specific growth rate and the glucose concentration under limited glucose, and then model equation was built. Besides, under two sole limited substrates, model equations of glucose consumption were built and comparison of the biomass yield, the growth maintenance coefficient were carried out.
结果表明：在葡萄糖限制条件下粪产碱杆菌的比生长速率与限制性底物浓度的关系符合Monod方程，建立了相应的模型方程；同时还建立了两种限制条件下的葡萄糖的消耗动力学模型；并对两种限制条件下的维持系数、菌体产率进行了比较。
In Chapter 6, the periodicity of continuous culture of microorganism in the turbidostat is discussed by investigating the existence of periodic solution of a kind of trubidostat model with impulsive state feedback control and Monod growth rate.
第6章研究了脉冲状态反馈控制对一类具有Monod增长率的恒浊器模型周期解存在性的影响，通过研究周期解的存在性来讨论微生物连续培养的周期性。
Olive oil co-substrate biodegradation with 200mg/L glucose can increase oil degradation rate by 8%～10%.
在油脂浓度≤2500mg／L时，X4菌对油脂的降解符合Monod动力学模型。
While the phenomenon of enzyme induction had been known for a long time, enzyme repression, the specific inhibition of enzyme synthesis, was not discovered until 1953, being reported simultaneously by the laboratories of Monod, Edward A.
在酶的诱导现象为人所知后很长一段时间，直到1953年酶合成的抑制现象即酶的阻遏才被发现，这是由伯克利的Monod ，Edward A。
Based on Michaclis-Menten zymic reaction kinetics, Monod model describing the relation between substrate concentration snd the specific growth rate of microor-ganism and microorgamism physiology given by Henkelekian etc., this.
以Michaclis-Menten的酶反应动力学和Monod关于基质浓度与微生物比增长速度之间关系的理论为指导，利用Henkelekian等人提出的微生物生理学理论推导了Lawrence-McCarty模式。
Correlations of specific growth rate of Acetobacter aceti using the extended Monod kinetics
应用扩展的Monod模型关联醋酸菌比生长速率
Degradative kinetics of pyrene and benzo [a] pyrene (BaP) in soil by six individual strains of fungi were examined using the Michaelis-Menton and Monod dynamic models.
研究了6株真菌对土壤中芘和苯并芘（BaP）的降解动态，用Michaelis-Menton和Monod动力学模型对结果进行拟合。
A new kinetics model for removing manganese by bio-oxidation is suggested by analyzing Monod equation.
通过分析莫诺得（Monod）方程，提出了一种新的反映生物氧化除锰规律的动力学模型。
Under test conditions, correlation coefficient of regression equation is more than 0.98, it shows that removing manganese by bio-oxidation did not follow up Monod equation but follows another reaction model.
试验条件下，回归方程的相关系数均在0.98以上，说明生物除锰不符合常见的Monod方程，而遵循另外一种反应动力学规律。
However, Monod-type kinetics is not able to describe the lag phase after inoculation or after pulse feeding.
然而，众所周知，Monod模型不能描述接种或补料操作后的细胞生长迟滞现象。
According to Monod Kinetic Equation, we calculated the kinetic data of of 7 substrates, and found that 7 kinds of substituted benzenes could be biodegraded in 12 hours, the biodegradability order is that: phenol benzoic acid benzene sulfonic acid toluene aniline chlorobenzene benzene.
结果发现经驯化后取代苯类化合物在12小时内都可以降解完全，一级生物降解速率常数的排序为：苯酚苯甲酸苯磺酸甲苯苯胺氯苯苯。
Monod coefficients (the maximum specific substrate utilization rate and half-saturation coefficient) and the yield coefficient Y are measured from batch experiments and fitted by least-square method.
描述生物降解过程的Monod参数（基质最大利用速率和半饱和常数）及生物得率通过间歇实验并用非线性最小二乘拟合获得。
To meet the urgent need of this technology in China, in the article three mathematical models of commonly used for artificial wetlands(First-order kinetic model, Monod kinetic model and Ergun formula) were discussed and the relations between the changes of expression were deduced in detail.
讨论了人工湿地3种常用的数学模型(一级动力学模型、Monod动力学模型和Ergun公式)，并对表达式之间的转换关系作了较为详细的推导；同时对其各自的优缺点作了分析。
The corrected formula of monod equation at the test temperature was:v=0.044(s-100)／[5719+(s-100)].it was also shown by the data from the test that the degradation of the butanediol-containing wastewater became stable when the retention time reached 40 hours.
结果表明monod方程的修正式能很好地描述丁二醇的降解规律，试验温度下monod方程的修正式为：v=0.044(s-100)/[5719+(s-100)]。试验数据还表明在停留时间达40h时，丁二醇废水的降解达到稳定。
Enzyme repression was discovered by Jacques Monod in 1953.
酶的阻遏作用是Monod于1953年发现的。