2, after which said mixture is thoroughly mixed, after which the process of making construction/finishing articles and structural structures from PM is performed by pouring PM in appropriate molds with subsequent vibration compaction, and/or additional pressing, and/or heating, or by extrusion.;EFFECT: technical result is higher efficiency and environmental friendliness of SMW recycling, reduced power consumption for SMW processing.;2 cl, 1 dwg"/> METHOD FOR ENVIRONMENTALLY SAFE AND WASTELESS RECYCLING OF REPRODUCED AND ACCUMULATED SOLID MUNICIPAL WASTES (SMW) USING MAGNESIA-BINDING SUBSTANCES AND INDUSTRIAL COMPLEX WITHOUT WASTES FOR ITS IMPLEMENTATION
首页> 外国专利> METHOD FOR ENVIRONMENTALLY SAFE AND WASTELESS RECYCLING OF REPRODUCED AND ACCUMULATED SOLID MUNICIPAL WASTES (SMW) USING MAGNESIA-BINDING SUBSTANCES AND INDUSTRIAL COMPLEX WITHOUT WASTES FOR ITS IMPLEMENTATION

METHOD FOR ENVIRONMENTALLY SAFE AND WASTELESS RECYCLING OF REPRODUCED AND ACCUMULATED SOLID MUNICIPAL WASTES (SMW) USING MAGNESIA-BINDING SUBSTANCES AND INDUSTRIAL COMPLEX WITHOUT WASTES FOR ITS IMPLEMENTATION

机译:使用含镁结合物和工业废料实现无害化,循环利用的累积和累积的固体城市废物(SMW)的环境安全和回收方法

摘要

FIELD: waste processing and disposal.;SUBSTANCE: group of inventions relates to recycling solid municipal wastes (SMW) and production of construction/finishing articles and structures. Disclosed is a method for nonwaste recovery of SMW and production of construction/finishing articles and building structures from "tailings" of processed SMW using magnesia-binding substances. Method comprises the following steps: delivery to receiving department of SMW, where preliminary or subsequent sampling of large-sized wastes (LSW) is performed with their further disassembly and handling, with obtaining of market-demanded secondary resources; then, separation (1st level of separation) of secondary resources suitable for subsequent use from supplied SMW in deep separation department, preliminary part of carbon-containing fractions SMW is selected for "cold pyrolysis" in power module for subsequent production of fuel products, which are further used to produce heat and electric energy for auxiliary needs of industrial complex ZW; further, OF SMW, including fine fractions, is fed into drying section; drying OF SMW is performed in automatic mode in a drying compartment at temperature of 160…200 °C with mixing at rotation of drying drums to 12…14 % moisture content, with water vapor discharge into atmosphere through ventilation pipes, wherein supply of heat energy to drying compartment is performed from own power module; then, OF SMW is supplied into grinding compartment with subsequent crushing and grinding of dried OF SMW of different morphological composition to fractions 0.1…6.0 mm; further, fractions with size of 0.1…6.0 mm on conveyor-vibration table (2nd stage of separation), wherein crushed and dried fractions during movement along conveyor-vibration table are intensely mixed with each other and as if jumping, at that, light fractions with powerful hot air flows are blown off into special containers, and heavy fractions remaining on the conveyor-vibratory table are further directed to the warehouse as a ready market product. Then one performs pulp preparation in the pulp preparation compartment, in the mixer hopper, where the light fractions are thoroughly mixed with the preserving NaCl brine and water added through the batcher to produce a homogeneous pulp; then, pulp is transported via pipelines to the pulp temporary storage location (PTSL) made in the form of reservoirs of vertical type. Pulp with PTSL, through into pulp distribution and transportation center, is directed for further processing. Pulp before its use in technological processes for production of construction/finishing articles and building structures, per 0.5…1.0 hour before its use, is activated to obtain a homogeneous mass, the molding mass of the PM, where into the pulp there added in ratio 1:1 magnesia-binding substances MgO and MgCl2, after which said mixture is thoroughly mixed, after which the process of making construction/finishing articles and structural structures from PM is performed by pouring PM in appropriate molds with subsequent vibration compaction, and/or additional pressing, and/or heating, or by extrusion.;EFFECT: technical result is higher efficiency and environmental friendliness of SMW recycling, reduced power consumption for SMW processing.;2 cl, 1 dwg
机译:领域:发明组涉及回收固体城市废物(SMW)以及建筑/装饰物品和结构的生产。本发明公开了一种利用表面活性剂结合镁的方法从表面处理过的SMW的“尾料”中回收SMW的无废料以及生产建筑/装饰制品和建筑结构的方法。该方法包括以下步骤:交付给SMW的接收部门,在该部门中,对大宗废物(LSW)进行初步或后续抽样,并进一步分解和处理,获得市场需求的二手资源;然后,从深层分离部门从供应的SMW中分离出适合后续使用的二次资源(第一层分离),将含碳馏分SMW的初级部分选择用于功率模块中的“冷热解”,以随后生产燃料产品。进一步用于生产热和电能,以满足工业园区ZW的辅助需求;此外,将包括细馏分的OF SMW进料到干燥段中; SMW的干燥是在温度为160…200°C的干燥箱中以自动模式进行的,同时在干燥鼓旋转的情况下进行混合,使其水分含量达到12…14%,水蒸气通过通风管排放到大气中,其中提供热能干燥室由自己的电源模块执行;然后,将OF SMW送入研磨室,随后将干燥后的具有不同形态组成的OF SMW压碎并研磨至0.1…6.0 mm的馏分;此外,输送机振动台上的尺寸为0.1…6.0 mm的馏分(分离的第二阶段),其中沿着输送机振动台移动时粉碎和干燥的馏分彼此强烈混合,就好像轻馏分在跳跃一样强劲的热气流被吹入特殊的容器中,而残留在输送机振动台上的重馏分则作为现成的市场产品被进一步送入仓库。然后,在混合器漏斗中的制浆室中进行制浆,将轻质馏分与保存的NaCl盐水和通过分批器添加的水充分混合,制成均匀的制浆;然后,纸浆通过管道输送到以垂直型储罐形式制成的纸浆临时存储位置(PTSL)。含PTSL的纸浆直接进入纸浆分配和运输中心,以进行进一步处理。在其使用前每0.5…1.0小时,将其用于制造建筑/装饰物品和建筑结构的工艺过程中的纸浆活化,以得到均质的物料,即PM的成型物料,并在其中按比例添加到纸浆中1:1氧化镁结合物质MgO和MgCl 2 ,然后将所述混合物充分混合,然后通过将PM倒入合适的模具中来执行由PM制成建筑/装饰物品和结构的过程。效果:技术成果是提高了SMW的回收效率和环境友好性,降低了SMW加工的能耗。2cl,1 dwg

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