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    • 4. 发明授权
    • Continuous process for complete removal or organic impurities from and
complete decolorization of prepurified wet-process phosphoric acid
    • 用于完全去除或有机杂质的连续方法和完全脱湿的湿法磷酸完全脱色
    • US4906445A
    • 1990-03-06
    • US311640
    • 1989-02-16
    • Gunther SchimmelGerhard BettermannGero HeymerFriedrich Kolkmann
    • Gunther SchimmelGerhard BettermannGero HeymerFriedrich Kolkmann
    • C01B25/234C01B25/235C01B25/46
    • C01B25/461C01B25/235
    • A continuous process is indicated for complete removal of organic impurities from and complete decolorization of pre-purified wet-process phosphoric acid which has been purified by an extractive method using an organic solvent, freed from residual hydrofluoric acid by steam stripping and treated with hydrogen peroxide at elevated temperature, which comprises mixing the pre-purified wet-process phosphoric acid and the hydrogen peroxide in a mixing zone at a temperature of from 100.degree. to 200.degree. C., preferably 140.degree. to 160.degree. C., and allowing them to react at this temperature for a further 1 to 4 hours, cooling to from 85.degree. to 90.degree. C. the pre-purified wet-process phosphoric acid treated in this way and pumping it at this temperature with exclusion of air firstly through an activated charcoal bed which has been prepared on the basis of peat and has been steam-activated and has a BET surface area of from 800 to 1000 m.sup.2 /g, and subsequently through a silicon carbide and/or graphite bed while maintaining a pumping rate of less than 0.5 m.sup.3 /h of wet-process phosphoric acid per m.sup.3 of activated charcoal bed.
    • 指示完全除去有机杂质并完全脱色预纯化的湿法磷酸的连续方法,其通过萃取方法使用有机溶剂纯化,通过汽提除去残留的氢氟酸并用过氧化氢处理 在高温下,其包括在预先纯化的湿法磷酸和过氧化氢的混合区中在100至200℃,优选140至160℃的温度下混合,并使它们 在该温度下再反应1至4小时,冷却至85℃至90℃,预纯化的湿法磷酸以此方式处理并在该温度下泵送,首先通过活性炭排除空气 基于泥炭制备并已蒸汽活化并具有800至1000m2 / g的BET表面积的床,随后通过碳化硅和/或石墨b 同时保持每立方米活性炭床的湿法磷酸的泵送速率小于0.5m 3 / h。
    • 5. 发明授权
    • Process for working up dusts which are produced in the electrothermal
production of phosphorus
    • 处理在电热生产中产生的粉尘的工艺
    • US4904459A
    • 1990-02-27
    • US385492
    • 1989-07-26
    • Friedrich KolkmannGunther SchimmelJohannes Scheffer
    • Friedrich KolkmannGunther SchimmelJohannes Scheffer
    • C01B25/027C01B25/30C01B25/41
    • C01B25/416C01B25/027C01B25/30
    • A process is provided for working up dusts which have been precipitated electrostatically from the gas mixture composed essentially of carbon monoxide and phosphorus vapor produced in the electrothermal production of yellow phosphorus, which process comprises converting the dusts into a calcinate at 300.degree. to 800.degree. C. under oxidizing conditions in a first step, leaching the calcinate with phosphoric acid in a second step, adjusting the pH of the solution in phosphoric acid to 0 to 1.5 with sodium hydroxide solution in a third step, precipitating the sulfides of lead, copper and cadmium from the partially neutralized solution in phosphoric acid by adding sulfide and filtering them off in a fourth step, adjusting the pH of the filtered, partially neutralized solution in phosphoric acid to about 1.5 to 5.0 with sodium hydroxide solution and precipitating zinc sulfide, if necessary by adding further quantities of sulfide, and filtering it off in a fifth step, further neutralizing the sodium phosphate solution, if necessary after expelling excess sulfide, with sodium hydroxide solution and separating it from precipitated calcium compounds in a sixth step, and using the resultant sodium phosphate solution in this form in a known manner to produce sodium phosphate salts.
    • 提供了一种处理从黄磷的电热生产中产生的基本上由一氧化碳和磷蒸气组成的气体混合物静电析出的灰尘的方法,该方法包括在300-800℃下将粉尘转化成煅烧物 在第一步骤的氧化条件下,在第二步中用磷酸浸出煅烧物,在第三步中用氢氧化钠溶液将磷酸溶液的pH调节至0至1.5,使铅,铜和 通过添加硫化物并在第四步骤中将其从磷酸中的部分中和的溶液中的镉,在氢氧化钠溶液中将过滤的,部分中和的磷酸溶液的pH调节至约1.5至5.0,如果需要,沉淀硫化锌 通过添加更多量的硫化物,并在第五步骤中过滤,进一步中和 磷酸二氢钠溶液,如果需要,用氢氧化钠溶液排出过量的硫化物,并在第六步骤中将其与沉淀的钙化合物分离,并以已知的方式使用所得的这种形式的磷酸钠溶液来生产磷酸钠盐。