首页> 外国专利> Treating liquid effluent supplied at rate of constant flow, comprises determining value of volume of reference, dividing volume into first and second digesters, inoculating second digester by microbial ecosystem, and dividing constant flow

Treating liquid effluent supplied at rate of constant flow, comprises determining value of volume of reference, dividing volume into first and second digesters, inoculating second digester by microbial ecosystem, and dividing constant flow

机译:处理以恒定流量供应的废水,包括确定参考体积的值,将体积分为第一和第二消化池,用微生物生态系统接种第二消化池以及划分恒定流量

摘要

The method comprises determining (20) a value of a volume of reference (V) of a reactor supplied with a constant flow (Q), dividing (30) the volume into a first digester of a first volume (V1) and a second digester of a second volume (V2) such that a sum of the first and second volumes is equal to that the volume of reference, inoculating (10) the second digester by a microbial ecosystem to convert a part of a substrate and to present an inhibition of growth by the substrate in an initialization phase, and dividing (40) the constant flow into a first flow and a second flow. The method comprises determining (20) a value of a volume of reference (V) of a reactor supplied with a constant flow (Q), dividing (30) the volume into a first digester of a first volume (V1) and a second digester of a second volume (V2) such that a sum of the first volume and the second volume is equal to that the volume of reference, inoculating (10) the second digester by a microbial ecosystem to convert a part of a substrate and to present an inhibition of growth by the substrate in an initialization phase, dividing (40) the flow into a first flow and a second flow such that the first flow supplies exclusively the first digester, and the second flow supplies initially second digester before being redistributed in the first digester. The method further comprises predetermining (11) a target value of concentration in the substrate, in which the first volume (V1=rV) is a percentage volume of reference with r as a parameter, the second volume (V2=(1-r)V) is percentage complementary to the volume of reference, the second flow (Q2=alpha Q) is a percentage of the rate of constant flow with alpha as a parameter, and the first flow (Q1= (1-alpha )Q) is complementary percentage to the rate of constant flow; determining (50) a dilution ratio of the second volume of the second digester and the dilution rate to be less than the value of the curve growth of the data on the microbial ecosystem for the given substrate; deducing a concentration value in the substrate corresponding to that of the dilution ratio from the growth curve; determining a set of values according to the value of the dilution rate and the value of the dilution ratio; choosing a subset of values from the determined set of values; determining a function representative of a speed or specific contribution in the substrate in the first digester at a given concentration based on a value of the parameter; selecting a value from the chosen values such that a variation curve of the function meets a graph of the function at more than one point; selecting a value from the chosen values such that the variation curve of the function does not meet a graph of the function at more than one point as the single point corresponds to a value of concentration in the weakest possible substrate; comparing the output concentration with the target value; and modifying the value of the parameter and/or the dilution ratio according to the result of the comparison. The volume of reference is equal to the rate of constant flow divided by a dilution rate, where the dilution rate is equal to a value of curve growth on microbial ecosystem data for the given substrate at a predetermined target value. An independent claim is included for an effluent treatment system.
机译:该方法包括确定(20)供应有恒定流量(Q)的反应器的参考体积(V)的值,将该体积划分(30)成第一体积(V1)的第一消化器和第二消化器第二体积(V2),以使第一体积和第二体积的总和等于参考体积,然后通过微生物生态系统接种(10)第二蒸煮器,以转化一部分底物并表现出抑制作用在初始化阶段通过衬底生长,并且将恒定流分成(40)第一流和第二流。该方法包括确定(20)供应有恒定流量(Q)的反应器的参考体积(V)的值,将该体积划分(30)成第一体积(V1)的第一消化器和第二消化器第二体积(V2)的体积,以使第一体积和第二体积的总和等于参考体积,然后向微生物消化系统接种(10)第二蒸煮器以转化一部分底物并呈现出在初始化阶段抑制基质的生长,将流分为(40)第一流和第二流,以使第一流仅供应第一消化器,第二流最初供应第二消化器,然后再重新分配到第一消化器中消化器。该方法还包括预先确定(11)基质中浓度的目标值,其中第一体积(V1 = rV)是参考体积的百分比,以r作为参数,第二体积(V2 =(1-r) V)是与参考体积互补的百分比,第二流量(Q2 = alpha Q)是以alpha为参数的恒定流量的百分比,而第一流量(Q1 =(1-alpha)Q)为恒定流量的互补百分比;确定(50)第二蒸煮器的第二体积的稀释率和稀释率小于给定底物的微生物生态系统上数据的曲线增长值;从生长曲线推导出对应于稀释比的底物浓度值;根据稀释率的值和稀释率的值确定一组值;从确定的一组值中选择一组值;基于所述参数的值确定代表给定浓度的第一消化器中的底物的速度或特定贡献的函数;从选择的值中选择一个值,以使函数的变化曲线在一个以上的点与函数的曲线图相交;从所选择的值中选择一个值,使得该函数的变化曲线在一个以上的点处不满足该函数的图,因为单个点对应于最弱的底物中的浓度值;比较输出浓度和目标值;根据比较结果修改参数值和/或稀释比。参考体积等于恒定流速除以稀释率,其中稀释率等于给定底物在预定目标值下在微生物生态系统数据上的曲线生长值。废水处理系统包括独立索赔。

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