英语翻译别用什么翻译软件来回答我!翻译好的继续加分.Results obtained for model sensiti
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英语翻译
别用什么翻译软件来回答我!翻译好的继续加分.
Results obtained for model sensitivity on maximum growth rate are shown in Fig.10.In this case,changes in mmax affects the ferrous iron oxidation in equal percentage to the variable modification in two cases studied.In Figs.11 and 12 results are shown for KS and KI,respectively.In general,it can be observed that these parameters have an important influence over ferrous iron oxidation rate in the bioreactors studied,but the type of influence is not equal in each model.In this way,
CSTR model is more sensible to changes in KS and ferrous iron oxidation calculated for packed-bed bioreactor has high sensitivity for changes in inhibition by product coefficient.
So,it is possible to establish an impact order:mmax_/
KS_/KI for CSTR and mmax_/KI_/KS for packed-bed bioreactor.
After that,the main aim of this study is to determine the ratio between the reaction rates in a continuous stirred tank reactor (rS(CSTR)) and that in a packed-bed bioreactor with immobilised biomass (rS(PB)) of T.
ferrooxidans as a function of the main process parameters:the input substrate concentration S0 and the substrate conversion.As we mentioned before,ferrous iron oxidation rate is equal to:A=BCD
and taking into account that the conversion is:B=ACD
Eq.(1) written in terms of substrate conversion,becomes:C=ABD
别用什么翻译软件来回答我!翻译好的继续加分.
Results obtained for model sensitivity on maximum growth rate are shown in Fig.10.In this case,changes in mmax affects the ferrous iron oxidation in equal percentage to the variable modification in two cases studied.In Figs.11 and 12 results are shown for KS and KI,respectively.In general,it can be observed that these parameters have an important influence over ferrous iron oxidation rate in the bioreactors studied,but the type of influence is not equal in each model.In this way,
CSTR model is more sensible to changes in KS and ferrous iron oxidation calculated for packed-bed bioreactor has high sensitivity for changes in inhibition by product coefficient.
So,it is possible to establish an impact order:mmax_/
KS_/KI for CSTR and mmax_/KI_/KS for packed-bed bioreactor.
After that,the main aim of this study is to determine the ratio between the reaction rates in a continuous stirred tank reactor (rS(CSTR)) and that in a packed-bed bioreactor with immobilised biomass (rS(PB)) of T.
ferrooxidans as a function of the main process parameters:the input substrate concentration S0 and the substrate conversion.As we mentioned before,ferrous iron oxidation rate is equal to:A=BCD
and taking into account that the conversion is:B=ACD
Eq.(1) written in terms of substrate conversion,becomes:C=ABD
对模型结果进行了敏感性最高增长率都显示在图10.在这种情况下,mmax变化影响的铁氧化亚铁百分比变量的改性两例进行研究.在无花果.第11和第12结果表明,气,分别为卡波西肉瘤.一般来说,它可以观察到这些参数有重要影响的亚铁氧化率铁箱型的研究,但不公平的影响模型.这样,
更明智,寻模型的变化规律,计算出铁氧化皇填充床生物反应器具有较高的敏感性,以产品为变化系数抑制.
所以,很有可能建立一个影响顺序:mmax _ /
卡波西肉瘤_ /气为寻mmax _ /亲吻,_ /皇填充床生物反应器.
在那之后,主要的目的是为了确定该研究的反应速率之间的比例在连续搅拌釜式反应器(rS),(寻在填充床生物反应器和固定生物量(拉尔夫-舒马赫(T)).
ferrooxidans的主要工艺参数:输入底物浓度对照和基质的转换.正如我们前面提到的,黑色铁氧化率等于:= BCD码
,考虑到转换为:B组分= ACD)
情绪智商.(1)中底,变成:C /转换、密
更明智,寻模型的变化规律,计算出铁氧化皇填充床生物反应器具有较高的敏感性,以产品为变化系数抑制.
所以,很有可能建立一个影响顺序:mmax _ /
卡波西肉瘤_ /气为寻mmax _ /亲吻,_ /皇填充床生物反应器.
在那之后,主要的目的是为了确定该研究的反应速率之间的比例在连续搅拌釜式反应器(rS),(寻在填充床生物反应器和固定生物量(拉尔夫-舒马赫(T)).
ferrooxidans的主要工艺参数:输入底物浓度对照和基质的转换.正如我们前面提到的,黑色铁氧化率等于:= BCD码
,考虑到转换为:B组分= ACD)
情绪智商.(1)中底,变成:C /转换、密
英语翻译别用什么翻译软件来回答我!翻译好的继续加分.Results obtained for model sensiti
英语翻译用翻译软件的别来
英语翻译,用翻译软件的别来
英语翻译请准确恰当的翻译,别拿翻译软件蒙我.有的是分,谁翻译的好就给谁加分.
求英语好的高手帮忙翻译,别拿软件翻译的来回答,谢谢
英语翻译别用翻译软件的翻译.
英语翻译翻译好了加分,别用软件打发我···
英语翻译我也有翻译软件,请不要用翻译软件来回答这个问题。
英语翻译别用软件翻译
英语翻译翻译得好的我加分.
英语翻译拜托别用翻译软件翻译,那是错的。
英语翻译注意:不要用翻译软件,那种东西不准确,我也有,翻译得好的加分~This is a temporary faq i