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Furnace for making high abrasion furnace black or intermediate super abrasion furnace black and process of operating same

机译:高耐磨炉黑或中级超耐磨炉黑的炉及其操作方法

摘要

1,147,884. Carbon black furnace. PHILLIPS PETROLEUM CO. 20 April, 1966 [23 April, 1965], No. 17331/66. Heading C1A. A carbon black furnace comprises a cylindrical combustion section (13) having an axial hydrocarbon feed inlet (59) and a preferably tangential fuel inlet (24), and two cylindrical reaction sections (14 and 16) with quench inlets (17 and 18) at their ends, the diameters of the respective sections being at least 2d, d, and (1 1/6-1 2/3)d, and the lengths of the reaction sections being 4¢-5¢ ft., and 8-11 ft., respectively. Suitable diameters for the three sections are 3“ ft., 1 ft. and 1“ ft., respectively. In Fig. 6, hydrocarbon feed from line 43 is preheated at 42 and passed via line 52 to nozzle 59, optionally with additives, e.g. aqueous KCI, from tank 61. Fuel hydrocarbon is passed from line 64 to nozzles 31 in inlets 24; alternatively, the hydrocarbon feed may be used as fuel by opening valve 32. Compressed air from line 39 is preheated at 38 and passed via line 53 to nozzles 29 to burn with the fuel. Some air may be passed via 63 to annular space 12 round nozzle 59. In furnace 11, the hydrocarbon feed is enveloped in an annular stream of hot combustion gas, and yields ISAF black if quenched with water at 17, or HAF black if quenched at 18. The quenches 17 and 18 may have 2 and 4 radial inlets respectively. The product stream is passed through indirect heat exchangers 37 and 41 (to preheat feed and air) and thence to bag filter 46. The hydrocarbon feed is preferably a light oil, e.g. petroleum, coal tar or synthetic gas oil or cracked residue, of specified properties. Particle size and surface area of the product are given.
机译:1,147,884。炭黑炉。 PHILLIPS PETROLEUM CO。,1966年4月20日[1965年4月23日],第17331/66号。标题C1A。炭黑炉包括具有轴向碳氢化合物进料口(59)和最好是切向燃料入口(24)的圆柱形燃烧段(13),以及两个带有淬火入口(17和18)的圆柱形反应段(14和16)。两端的直径至少为2d,d和(1/1 / 6-1 2/3)d,反应部分的长度为4¢-5¢ft。,且为8-11英尺。这三个部分的合适直径分别为3“ ft。,1 ft。和1” ft.。在图6中,将来自管线43的烃进料在42处预热并经管线52送至喷嘴59,任选地加入添加剂,例如添加剂。燃料碳氢化合物从管线64进入入口24的喷嘴31;燃料KFC则从罐61流出。或者,可通过打开阀32将烃类进料用作燃料。来自管线39的压缩空气在38处预热,并通过管线53到达喷嘴29,与燃料一起燃烧。某些空气可通过63穿过圆形喷嘴59进入环形空间12。在炉11中,碳氢化合物进料被包裹在环形的热燃烧气体流中,如果用水在17淬灭,则产生ISAF黑色,如果在17淬灭则生成HAF黑色。 18.骤冷器17和18可以分别具有2个和4个径向入口。产物流通过间接热交换器37和41(以预热进料和空气),然后到达袋式过滤器46。烃进料优选为轻油,例如轻油。具有特定性能的石油,煤焦油或合成瓦斯油或裂化残渣。给出了产品的粒度和表面积。

著录项

  • 公开/公告号GB1147884A

    专利类型

  • 公开/公告日1969-04-10

    原文格式PDF

  • 申请/专利权人 PHILLIPS PETROLEUM COMPANY;

    申请/专利号GB19660017331

  • 发明设计人

    申请日1966-04-20

  • 分类号C09C1/48;C09C1/50;

  • 国家 GB

  • 入库时间 2022-08-23 11:52:26

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