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The process of producing ferric oxide from waste iron mud in dye factory with calcination has been studied.

研究了以染化厂产生的废料铁泥为原料,采用烧法生产氧化铁红颜料的工艺,简要介绍了该法生产氧化铁红的反应机理及温度、酸度、烧时间对产品质量的影

A new recovery technology of solid waste was made which is from furfuryl alcohol production by furfural hydrogenization. When the solid waste is placed in a vacuum drying box, and is under lower negative pressure and at 130℃, the organic materials in solid waste can be distilled and then returned to the refining workshop to produce qualified furfuraldehyde and furfuryl alcohol. The remainder is mixed with soda ash and roasted in a reverberating furnace. The sodium chromate can be obtained by leaching. Rough cupric oxide is dissolved in nitric acid and cupric nitrate is obtained. A new catalyst was prepared by the above sodium chromate and cupric nitrate and used in furfuryl alcohol production.

将糠醛液相加氢生产糠醇产生的废渣置于真空干燥箱中,在较低的负压状态下保持130℃的温度,蒸馏回收废渣中的有机物,返回糠醇精制车间获得合格的糠醇与糠醛产品;剩余的固体废弃物与纯碱混合,在反射炉中烧,浸取获得铬酸钠水溶液;最后剩下的粗氧化铜溶于硝酸得到硝酸铜溶液;将铬酸钠溶液、硝酸铜溶液按一定比例混合,加入氨水搅拌,分离出的沉淀经传统方法烧活化、造粒制得新催化剂,回用于糠醛液相加氢生产糠醇。

The experiment results show that the induration energy cost will be reduced 10-30% with the advanced firing system under the same raw material conditions.

在同样的原燃料条件下,与现有的烧制度相比,作者提出的新型烧制度能节省能耗10-30%。

The catalyst on calcination temperature of 400℃ had the highest conversion of isobutylene and the catalyst on calcination temperature of 500℃ had the highest selectivity of methacrolein .

烧温度为400℃的催化剂异丁烯的转化率最高,烧温度为500℃的催化剂甲基丙烯醛的选择性最高。

The results show that when the mass ratio of sodium jarosite residue to anthracite is 5∶1, reduction roast lasts at 800℃for 0.5 h, leaching is carried out at 70℃for 40 min by 0. 5 mol/L H2SO4 with liquid-solid ratio of 7∶1, 93% of both iron and nickel can be leached out.

研究结果表明:当黄钠铁矾渣与无烟煤按质量比为5∶1均匀混合,在800℃还原烧0.5 h,烧渣用0.5 mol/L硫酸溶液按液固比7∶1在70℃浸出40 min时,渣中93%的铁和镍进入浸出液中。

The results show that when the mass ratio of sodium jarosite residue to anthracite is 5:1, reduction roast lasts at 800℃ for 0.5 h, leaching is carried out at 70℃ for 40 mm by 0.5 mol/L H2SO4 with liquid-solid ratio of 7:1, 93% of both iron and nickel can be leached out.

研究结果表明:当黄钠铁矶渣与无烟煤按质量比为5:1均匀混合,在800℃还原烧0.5h,烧渣用0.5mol/L硫酸溶液按液固比7:1在70℃浸出40min时,渣中93%的铁和镍进入浸出液中。

This paper studies the neutralize agent for zinc hydrometallurgy of jarosite process,analyses advantage and disadvantage of NH_4HCO_3 and calcine as jarosite precipitation neutralize agent,points out if used calcine removed zinc ferrite as neutralize agent,than can cut the cost and reduce zinc content in slag.

研究了湿法炼锌黄钾铁矾渣除铁工艺的中和剂,分析了碳酸氢铵和砂作为沉矾中和剂的优缺点,指出用除去铁酸锌的砂作中和剂,可降低成本,减少渣含锌。

This paper analyzes the reason of effects masonry of roasting furnace, and puts forward improving plan .

对影响烧炉砌筑的原因进行分析,并提出了烧炉砌筑工艺改进方案。

The best performance for Sw: 1 Al' mole ratio calcination temperature, curing time 650 qC Rao 3 h: citric acid catalytic Taiwan into the best condition of isooctyl catalyst for: 1 (2%), the total alcohol acid mellowly Moore j l: 5 than when asked 2 h.

烧温度650 qC。娆时间3 h:催化台成柠檬酸异辛酯的最佳条件为:催化剂用量1 2%,酸醇摩尔比l:5。

Using concentrate containing Mo≥54% as precursor,by advanced roasting furnace for oxidization roasting molybdenite concentrate can produce high quality technical molybdenum oxide possessed of world grade.

只有以含钼≥54%、杂质低的钼精矿作生产工业氧化钼的前驱体,采用较先进的烧设备进行氧化烧才能产出与国际钼市场产品质量接轨的工业氧化钼产品。

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