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    • 1. 发明专利
    • Preparation of coal/water slurry
    • 煤/水浆的制备
    • JPS58213096A
    • 1983-12-10
    • JP9612782
    • 1982-06-07
    • Babcock Hitachi KkHitachi Ltd
    • MURANAKA TADASHIKAJI RIYUUICHIKIKUCHI HIDEOAKIMOTO HIDETOSHIOOTSUKA KEIZOU
    • C10L1/32C10L5/00C10L9/00
    • PURPOSE: To prepare a coal/water slurry of high concentration, low viscosity and low ash content, by crushing raw material coal into a plurality of ground coals having different particle size distributions, deashing them separately and blending the refined coals.
      CONSTITUTION: In the preparation of a coal/water slurry of high concentration, low viscosity and low ash content in which raw material coal is crushed, classified by particle diameter and deashed, a plurality of ground coals with different particle size distributions are produced by crushing the raw material coal in coarse, medium and fine sizes. The ground coals are deashed separately into refined coals, which are classified by particle diameter. The refined coals are blended for adjustment of particle diameter and made into concentrated aqueous slurry of coal. Although a larger maximum particle diameter and a wider range of particle diameter distribution afford a higher concentration of slurry, coal particles with a diameter of 300μm or larger are difficult to burn and therefore the maximum particle diameter of adjusted coal should be 300μm at largest.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:为了制备高浓度,低粘度和低灰分含量的煤/水浆料,通过将原料煤粉碎成具有不同粒度分布的多个地煤,将它们分开排出并混合精炼煤。 构成:在制备原料煤粉碎的高浓度,低粘度和低灰分含量的煤/水浆料中,通过粒径分级和分级,通过粉碎生产多种不同粒度分布的煤, 原料煤粗,中,细尺寸。 地煤被分开分解成精细煤,根据粒径分类。 将精制煤混合以调节粒径并制成煤的浓缩含水浆料。 虽然较大的最大粒径和较宽的粒径分布范围提供了更高浓度的浆料,但是直径为300μm或更大的煤颗粒难以燃烧,因此调整煤的最大粒径最大应为300μm。
    • 8. 发明专利
    • FILLING LAYER REACTION APPARATUS
    • JPS5624037A
    • 1981-03-07
    • JP9720179
    • 1979-08-01
    • HITACHI LTDBABCOCK HITACHI KK
    • ARASHI NORIOAKIMOTO HIDETOSHIGOMI KENICHIKOMURO TAKEOHISHINUMA TAKAONAKASHIMA FUMITO
    • B01D53/08B01J8/08B01J8/12C25D1/02
    • PURPOSE:To enhance the utilization ratio of an adsorbing agent in a filling layer by a method wherein a solid adsorbing filled layer is supported in a movable manner in an air permeable support having a throwing port and a withdrawing port provided to an upper and a lower portion therein and the above described filling layers are arranged in parallel in a gas stream at a predetermined intervals. CONSTITUTION:In the titled apparatus for adsorbing and removing a specific component contained in a gas containing dusts by a solid adsorbing agent, a solid adsorbing agent filled layer 6 is supported in a movable manner in an air permeable support having a throwing apparatus 13 and a withdrawing apparatus 15 provided to an upper and a lower portion in a reaction tube 7 and this filled layer 6 is arranged in parallel in a gas flowing passage at a predetermined distance. In this time, the thickness of above described filled layer 6 is adjusted to 5-30 times of an average particle diameter of the adsorbing agent and the adsorbing agent 6 moving downwardly is heated in a heating portion 11 to desorb an adsorbed component and this desorbed component is removed by a purge gas 12. A regenerated adsorbing agent is circulated and used through the withdrawing device 15. Thereby, the thickness of the filled layer 6 can be enlarged so as to be able to utilize up to the central portion thereof.