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System for and method of destroying aqueous slurries containing combustible organic waste materials

机译:销毁含有可燃有机废料的水浆的系统和方法

摘要

1,030,231. Burning refuse. GENERAL AMERICAN TRANSPORTATION CORPORATION. Feb. 6, 1963 [March 12, 1962], No. 4804/63. Heading F4B. An aqueous slurry containing combustible organic waste is burnt in a bed of refractory material 130 which is fluidized by an inlet stream of oxygen containing gas and maintained at such a temperature that the water in the slurry is evaporated and the waste burned within the bed. The fluidized bed 130 is supported on a lower layer of coarse fire brick 130a resting on a refractory grate 131. Air is delivered to a lower chamber 102a and passes to a chamber 102b containing a burner 193 to raise the temperature of the bed 130 for starting the process. The steam and gases from the bed 130 are completely burned in an upper part 120 of greater diameter than the bed 130, and pass through a dust separator 180 (Fig. 2, not shown), to the inner tube of a heat exchanger 270 which heats the combustion air. The gases pass through fresh slurry in an evaporator 240 to a condenser and stack (Fig. 3, not shown). The slurry, which may be sewage sludge mixed with ground garbage, is passed through screens to remove oversize solids and a mixer to the evaporator 240, where a sludge containing 3-10% by weight of combustible solids is concentrated to give a sludge containing 8-25% by weight of solids. By regulating the supply of sludge and air, the temperature of the fluidized bed can be maintained at between 1,300-1,800‹ F. without the further use of the burner 193.
机译:1,030,231。燃烧垃圾。通用美国运输公司。 1963年2月6日[1962年3月12日],编号4804/63。标题F4B。含有可燃有机废物的含水浆料在耐火材料层130中燃烧,该耐火材料层130通过含氧气体的入口流而流化并保持在这样的温度下,使得浆料中的水蒸发并且废物在该层中燃烧。流化床130被支撑在搁在耐火炉resting131上的粗耐火砖130a的下层上。空气被输送到下部腔室102a,并通向包含燃烧器193的腔室102b,以升高床130的温度以启动过程。来自床130的蒸汽和气体在直径大于床130的上部120中完全燃烧,并通过灰尘分离器180(图2,未示出)到达热交换器270的内管。加热燃烧空气。气体通过蒸发器240中的新鲜浆料到达冷凝器和烟囱(图3,未示出)。将可能是污水污泥与地面垃圾混合的淤浆通过筛网以去除过大的固体,然后将混合器送至蒸发器240,在蒸发器240中浓缩含有3-10%重量百分比的可燃固体的污泥,从而得到含有8%污泥的污泥。固体重量的-25%。通过调节污泥和空气的供应,流化床的温度可以保持在1,300-1,800°F之间,而无需进一步使用燃烧器193。

著录项

  • 公开/公告号GB1030231A

    专利类型

  • 公开/公告日1966-05-18

    原文格式PDF

  • 申请/专利权人 GENERAL AMERICAN TRANSPORTATION CORPORATION;

    申请/专利号GB19630004804

  • 发明设计人

    申请日1963-02-06

  • 分类号F23G5/30;F23G7/00;

  • 国家 GB

  • 入库时间 2022-08-23 14:44:06

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