通过对铬浸出渣资源综合利用试验可得通过浸出试验可得Cr6+平均浸出率为

通过对铬浸出渣资源综合利用试验可得通过浸出试验可得Cr6+平均浸出率为99.94%，∑Cr平均浸出率为86.55%，Fe平均浸出率为94.72%。通过萃取-反萃取-沉淀工序可以获得99%以上的氢氧化铁和98.5%以上氢氧化铬；通过萃余液处理工艺试验，获得符合工业标准的主品位97%以上的硫酸钙(晶须)、40%以上的碳酸镁和98%以上的工业氯化钠，处理后的萃余液返回浸出工序循环使用，实现了副产盐酸和铬资源的综合利用。

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结果 (英语) 1: [复制]

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Through the utilization of resources test chromium leaching residue can be prepared by leaching tests available Cr6 + average leaching rate of 99.94%, ΣCr average leaching rate of 86.55%, Fe average leaching rate of 94.72%. By extraction - trans extraction - precipitation step can be obtained more than 99% or more and 98.5% iron hydroxide, chromium hydroxide; raffinate by treatment process test, obtain the primary industry standard grade of 97% or more of calcium sulfate (whiskers) , more than 40% of magnesium carbonate and 98% sodium chloride industry, the raffinate recycle process returns leaching step, to achieve a product hydrochloric acid and chromium utilization of resources.

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结果 (英语) 2:[复制]

复制成功！

The average leaching rate of Cr6 plus leaching by the leaching test can be obtained by the comprehensive utilization test of chromium leaching resources, the average leaching rate of Cr Cr is 86.55%, and the average Leaching rate of Fe is 94.72%. More than 99% of iron hydroxide and more than 98.5% chromium hydroxide can be obtained through extraction-reverse extraction-precipitation process, and more than 97% calcium sulfate (whiskey) of the main grade in line with industrial standards, magnesium carbonate of more than 40% and more than 98% of industrial sodium chloride can be obtained through the extraction and solution process tests. The processd extract is returned to leaching process for recycling, which realizes the comprehensive utilization of by-product hydrochloric acid and chromium resources.

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结果 (英语) 3:[复制]

复制成功！

Through the comprehensive utilization of chromium leaching residue resources, the average leaching rate of Cr6 + is 99.94%, the average leaching rate of Σ Cr is 86.55%, and the average leaching rate of Fe is 94.72%. More than 99% Fe (OH) 2 and more than 98.5% Cr (OH) 2 can be obtained by the extraction reverse extraction precipitation process; more than 97% of calcium sulfate (whisker), more than 40% of magnesium carbonate and more than 98% of industrial sodium chloride can be obtained by the treatment process of the raffinate, and the raffinate after treatment can be returned to the leaching process for recycling, realizing the by-product of hydrochloric acid and chromium resources Comprehensive utilization.<br>

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