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    • 1. 发明申请
    • SELF-SUSTAINABLE ZERO INFLUENT AND ZERO DISCHARGE WASTE TO ENERGY SYSTEM AND METHOD FOR TREATING SUGAR INDUSTRY EFFLUENT AND DISTILLERY SPENT WASH
    • 自主可持续的零度影响和零排放废物处理能源系统及方法,用于处理糖类工业废水和废物清洗
    • WO2013069026A1
    • 2013-05-16
    • PCT/IN2012/000209
    • 2012-03-29
    • TRANSCARB ENERGY PRIVATE LIMITEDVIJAY, Kumar NarayanKRISHNAN, NeelakantanPRADEEP, KuberSUBASH, Mathurvaishya
    • VIJAY, Kumar NarayanKRISHNAN, NeelakantanPRADEEP, KuberSUBASH, Mathurvaishya
    • C02F3/28C02F9/14C02F9/04C02F9/08
    • C02F1/441C02F3/286C02F2103/32C02F2303/10C12M21/04C12M23/58C12M47/18Y02E50/343Y02P20/59Y02W10/30
    • A self-sustainable zero influent and zero discharge waste to energy system and method for treating sugar factory effluent, press mud, and distillery spent wash, said system comprises: first Biomethanation and Anaerobic Digestion Module adapted to receive sugar factory effluent, press mud, and reverse osmosis reject water for obtaining biogas and organic digestate; second Biomethanation and Anaerobic Digestion Module adapted to receive distillery spent wash and liquid filtrate from Micro Strainer for obtaining biogas and dilute organic liquid effluent digestate; Biogas Cleanup Module for converting hazardous hydrogen sulphide in the biogas into elemental sulphur, and moisture-free Dry biogas; Biogas Engine Generator Module for producing electrical power, hot exhaust gas and hot water; Biogas Engine Exhaust Gas Waste Heat Recovery Module for producing Steam, and cooled exhaust gas for expulsion into atmosphere; Solid Fuel Module for producing solid fuel for a co-generation plant, liquid filtrate from Micro strainer for said second Biomethanation and Anaerobic Digestion Module; Hot condensate water from Solid Fuel Dryer returned in close loop to said Biogas Engine Exhaust Gas Waste Heat Recovery Module for producing steam; and Reverse Osmosis Waste Water Treatment Module for obtaining filtered effluent for reverse osmosis unit which outputs a first predefined portion of reverse osmosis, usable water and a second remainder predefined portion of reverse osmosis reject effluent as feed to first Biomethanation and Anaerobic Digestion Module.
    • 该系统包括:第一个生物甲烷化和厌氧消化模块,适用于接收糖厂废水,压浆,和 反渗透废水用于获得沼气和有机消化; 第二个生物甲烷化和厌氧消化模块适用于从微过滤器接收酿酒废液和液体滤液,以获得沼气和稀释有机液体废液消解物; 用于将沼气中有害硫化氢转化为元素硫的沼气净化模块,以及无湿干燥沼气; 用于生产电力,热排气和热水的沼气发动机发电机模块; 用于生产蒸汽的沼气发动机废气余热回收模块,用于排入大气的冷却废气; 用于生产用于共发电厂的固体燃料的固体燃料模块,用于所述第二生物甲烷化和厌氧消化模块的Micro过滤器的液体滤液; 来自固体燃料干燥器的冷凝水冷水返回到用于生产蒸汽的沼气发动机废气余热回收模块; 和反渗透废水处理模块,用于获得用于反渗透单元的过滤流出物,其将第一预定义的部分反渗透输出,可用水和第二剩余部分预反应的部分反渗透排出物作为第一生物降解和厌氧消化模块的进料。