首页> 外国专利> PROCESS FOR RECOVERING PIGMENTARY TITANIUM DIOXIDE FROM NONPIGMENTARY WASTE TITANIUM DIOXIDE

PROCESS FOR RECOVERING PIGMENTARY TITANIUM DIOXIDE FROM NONPIGMENTARY WASTE TITANIUM DIOXIDE

机译:从非食用二氧化钛中回收二氧化钛的方法

摘要

1,140,029. Titanium dioxide. PPG INDUSTRIES Inc. 28 Feb., 1966 [18 March, 1965], No. 8601/66. Heading C1A. The tinting strength of non-pigmentary TiO 2 produced by vapour phase oxidation of Ti halide is increased by screening a slurry of the TiO 2 having a pH of 6-12 to remove particles greater than 90 Á in diameter, milling the slurry until the particles are all less than 10Á in diameter, and hydrocycloning the slurry. The slurry may have a solids content of 30-65% by wt. and a viscosity of 100-2500cp., and may contain 0À05-0À5% by wt. based on the wt. of oxide, of a dispersant, e.g. Na, K, Li, or NH 4 hypophosphate, hypophosphite, orthophos - phates, metaphosphates, pyrophosphate, or tripolyphosphate, NaNH 4 phosphate, ethylene diamine, ethylamine, diethanolamine, diethylene triamine, pyridine, triethylamine, or benzyl trimethyl ammonium hydroxide. The pH of the slurry may be adjusted by adding NaOH, KOH, LiOH, NH 4 OH, Ca(OH) 2 , BaCO 3 , K 2 CO 3 , Na 2 CO 3 , KHCO 3 ,NaHCO 3 , or NaOH + Na 2 CO 3 . The slurry may be ball-milled for 5 mins-36 hrs, and then diluted to a solids content of 15-25% by wt and hydroclassified to give a fine fraction having a particle size of less than 0À4Á. The non-pigmentary TiO 2 has a tinting strength of less than 1200 and is the material scraped from the walls of the oxidation reactor or removed from the bed particles in a fluidized bed process by milling. It may contain 0À1-10% by wt of another oxide, preferably Al 2 O 3 (an exhaustive list of other oxides is given).
机译:1,140,​​029。二氧化钛。 PPG INDUSTRIES Inc. 1966年2月28日[1965年3月18日],第8601/66号。标题C1A。通过筛分pH值为6-12的TiO 2浆料以去除直径大于90的颗粒,将浆料研磨直至颗粒,从而提高了卤化钛卤化物气相氧化产生的非颜料TiO 2的着色强度。直径均小于10Á,并对浆液进行水力环流。浆料可具有30-65重量%的固体含量。粘度为100-2500cp。,可以包含0-05-0-5%重量。基于重量氧化物,分散剂如Na,K,Li或NH 4次磷酸盐,次磷酸盐,正磷酸盐,邻磷酸盐,焦磷酸盐或三聚磷酸盐,NaNH 4磷酸盐,乙二胺,乙胺,二乙醇胺,二亚乙基三胺,吡啶,三乙胺或苄基三甲基氢氧化铵。可通过添加NaOH,KOH,LiOH,NH 4 OH,Ca(OH)2,BaCO 3,K 2 CO 3,Na 2 CO 3,KHCO 3,NaHCO 3或NaOH + Na 2来调节浆料的pH。 CO 3。可以将浆液球磨5分钟-36小时,然后稀释至15-25%wt的固含量,并进行水分级以得到粒度小于0-4A的细级分。非颜料TiO 2的着色强度小于1200,是在流化床工艺中通过研磨从氧化反应器壁刮下或从床颗粒中除去的材料。它可以包含0-1.10%(重量)的另一种氧化物,最好是Al 2 O 3(给出了其他氧化物的详尽清单)。

著录项

  • 公开/公告号JPS4917959B1

    专利类型

  • 公开/公告日1974-05-07

    原文格式PDF

  • 申请/专利权人

    申请/专利号JP19660016204

  • 发明设计人

    申请日1966-03-17

  • 分类号C01G23/00;C09C1/36;

  • 国家 JP

  • 入库时间 2022-08-23 06:20:04

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