首页> 外国专利> Granular activated carbon manufacture from low rank agglomerating but not good coking bituminous coal treated with dilute inorganic acid

Granular activated carbon manufacture from low rank agglomerating but not good coking bituminous coal treated with dilute inorganic acid

机译:用稀无机酸处理的低级团聚而不是优质焦化烟煤制粒状活性炭

摘要

Granular activated carbon is manufactured from low rank agglomerating but not good coking bituminous coal by crushing and screening the as received coal to produce 8/30 mesh granules, which are treated with a dilute aqueous solution of inorganic acid to prevent fusion of the granules during subsequent devolatilization comprising: mixing the granules with the acid (H.sub.2 SO.sub.4, H.sub.3 PO.sub.4, HCl or mixtures thereof) at a concentration of about 1% to about 15% by weight, washing off the acid, drying the granules thoroughly and thereafter mixing the granules with about 5 to about 15% by weight of a carbonaceous binder such as coal tar pitch. The so treated granules are ground to at least about 65% by weight -325 mesh powder, which is compressed into shapes such as pellets of 0.5 inch diameter and 0.5 inch long under a pressure of 40,000 to 80,000 psi, and then granulated to obtain 6/20 mesh granules. These granules are first charred by heating to 250 C at 150 C/hour in an atmosphere of air and nitrogen and by maintaining the temperature for 4 hours, next devolatilized by heating to 450 C at 300 C/hour in an atmosphere of N.sub.2 and the volatiles and by maintaining the temperature for 1 hour, and then activated by heating to 800 to 900 C in an atmosphere of N.sub. 2 and steam and by maintaining the temperature for 4 to 5 hours. The activated granules have a surface area of 1050 to 1090 m.sup.2 /gram, an Iodine number of 900 to 1100, an ash content of 6 to 9%, an abrasion number 75 to 80, and an apparent density of 0.51 to 0.53 gram/cc, which properties make them suitable for use in water and waste water treatment and in other applications.
机译:粒状活性炭是由低级聚结但焦化效果不佳的烟煤制成的,方法是将原煤破碎并过筛,以生产8/30目颗粒,然后用稀无机酸水溶液处理,以防止颗粒在随后的熔化过程中熔化。脱挥发分包括:将颗粒与浓度为约1%至约15%重量的酸(H.sub.2 SO.4,H.sub.3 PO.4,HCl或它们的混合物)混合,洗去酸,彻底干燥颗粒,然后将颗粒与约5至约15重量%的碳质粘合剂如煤焦油沥青混合。将如此处理的颗粒研磨成至少约65%重量的-325目粉末,将其在40,000至80,000 psi的压力下压缩成诸如0.5英寸直径和0.5英寸长的粒料的形状,然后造粒以获得6。 / 20目颗粒。这些颗粒首先通过在空气和氮气气氛中以150℃/小时加热至250℃并保持温度4小时而被烧焦,然后通过在N.sub气氛中以300℃/小时加热至450℃而挥发掉。 .2和挥发物并通过保持温度1小时,然后通过在N 2气氛中加热至800至900℃而活化。 2,通入蒸汽并通过保持温度4至5小时。活化的颗粒的表面积为1050至1090m 2 /克,碘值为900至1100,灰分为6至9%,磨耗值为75至80,表观密度为0.51至100。 0.53克/立方厘米,该特性使其适用于水和废水处理以及其他应用。

著录项

  • 公开/公告号US4131566A

    专利类型

  • 公开/公告日1978-12-26

    原文格式PDF

  • 申请/专利权人 THE CARBORUNDUM COMPANY;

    申请/专利号US19770818699

  • 发明设计人 HARI N. MURTY;

    申请日1977-07-25

  • 分类号C01B31/10;C01B31/08;B01J21/18;

  • 国家 US

  • 入库时间 2022-08-22 19:21:41

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