首页> 外国专利> Procedure for washing and Dilution of the colprocedimiento for washing and Dilution of ore Tailings in the process of acid Leach of ore in the process of acid Leach ores and Minerals lateru00cdticos lateru00cdticos

Procedure for washing and Dilution of the colprocedimiento for washing and Dilution of ore Tailings in the process of acid Leach of ore in the process of acid Leach ores and Minerals lateru00cdticos lateru00cdticos

机译:酸性浸出矿石和矿物过程中矿石浸出过程的洗涤和稀释过程的协同稀释法矿石和矿物的浸出过程随后的过程

摘要

The Procedure for washing and Dilution of the procedure for washing and Dilution of ore Tailings in the leaching process u00e1cidcolas ore in the process of acid leaching of laterite ores associated with laa is lateritic Minerals. Na with the domestic Metallurgical Industry and in particular with the Branch and in particular with the Metallurgical IndustryThe Nickel and Cobalt. The Procedure consisted of nickel and Cobalt.The Procedure consists in mixing, residual Water in Mixing - deshumide scrubber, Scrubber Wastewater dehumidifier with a suspension of coificador Tail ore, with an ore Tail suspension with a 25 - 50% Solids, in a ratio of 0, n a 25 - 50% of all Solid, in a ratio of 0.3 - 3 liters of water / liters of Liquor EN3 - 3 liters of water / liters of liquor in the suspension Lines, during 1 - Suspension of queues, during 1 to 5 minutes, with a moderada5 minutes agitation intensity,With a moderate intensity of agitation (Re: 10000 - 12000) and a temperature of 313 - (Re: 10000 - 12000) and a temperature of 313 - 378 K. this work can be applied in empresas378 K.This work can be applied in companies producing nickel and Cobalt by L producing nickel and Cobalt ore by leaching with sulfuric acid and preciixiviaciu00f3n ore with sulfuric acid and the precipitate dissolved Metals sulfide HID Ru00f3gepitan dissolved Metals with Hydrogen sulfide. Not.
机译:洗涤和稀释的程序浸出过程中的尾矿的洗涤和稀释程序是在与Laa结合的红土矿石的酸浸过程中的尾矿的洗涤和稀释程序是红土矿物。 Na与国内冶金工业,特别是与冶金科,特别是与冶金工业有关的镍和钴。该程序由镍和钴组成,包括以下步骤:混合,混合中的残留水-除湿洗涤塔,洗涤塔废水除湿机(带有Coificador尾矿的悬浮液),矿尾悬浮液(固体含量为25-50%),比例为0,不存在25-50%的所有固体,比率为0.3-3升水/升白酒EN3-3升水/升悬浮液中的白酒,在1-暂停排队期间1至5分钟,搅拌强度为5分钟,适度的搅拌强度(Re:10000-12000),温度为313-(Re:10000-12000),温度为313-378K。这项工作可用于L生产镍和钴矿石的公司,该公司通过用硫酸浸出镍和Preciixiviaci u00f3n矿石以及沉淀的溶解金属硫化物HID R u00f3gepitan溶解金属来生产镍和钴矿石。硫化氢。不。

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