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METHOD AND SYSTEM FOR METHANE FERMENTATION PROCESSING OF SLUDGE USING HYDROTHERMAL REACTIONS

机译:利用水热反应进行甲烷发酵污泥的方法和系统

摘要

Provided are a methane fermentation processing method and system capable of increasing the amount of methane gas recovered from sludge which has been previously processed by hydrothermal reactions. After sludge (S) has been concentrated to a prescribed moisture content by means of a concentration device (4), the concentrated sludge (S) is circulated for a prescribed amount of time between a hydrothermal reactor (11) and a gas-liquid separator (12) to reduce the molecular weight of the sludge while the same is heated to a hydrothermal temperature (T) so as to maximize the amount of methane gas recovered per unit amount of sludge resulting from methane fermentation processing. The low molecular weight sludge (S) is retained for a prescribed amount of time in a methane fermentation tank (20), and the methane gas (G) is recovered. Ideally, the hydrothermal temperature (T) is a temperature in the range 160-200°C which maximizes the amount of methane gas recovered per unit amount of sludge resulting from the methane fermentation processing, the low molecular weight sludge (S) is retained for 3-5 days in the methane fermentation tank (20), and the methane gas (G) recovered.
机译:提供了一种甲烷发酵处理方法和系统,该方法和系统能够增加从预先通过水热反应处理过的污泥中回收的甲烷气体的量。在利用浓缩装置(4)将污泥(S)浓缩至规定的水分含量之后,将浓缩的污泥(S)在水热反应器(11)与气液分离器之间循环规定的时间。 (12)降低污泥的分子量,同时将其加热到水热温度(T),以使甲烷发酵处理产生的每单位污泥的甲烷气回收量最大化。将低分子量污泥(S)在甲烷发酵罐(20)中保留规定的时间,并回收甲烷气体(G)。理想地,水热温度(T)是160-200°C范围内的温度,该温度可使甲烷发酵工艺产生的每单位污泥中回收的甲烷气体量最大化,而低分子量污泥(S)保留用于在甲烷发酵罐(20)中放置3-5天,并回收了甲烷气体(G)。

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