Iron removing method for pickle liquor during extraction of vanadium in stone coal
An acid leaching solution and stone coal technology, applied in the field of iron ion removal, can solve the problems of high reaction conditions and high investment costs, and achieve the effects of strong selectivity, less environmental pollution and reduced consumption.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0020] Use concentrated sulfuric acid at 90°C to continuously leaching stone coal for 8-10 hours, filter out solid impurities to obtain an acid leaching solution, adjust the pH value of the acid leaching solution to 2.00±0.02 with ammonia water, and the iron ion concentration is 0.206g at this time ·L -1 , vanadium ion concentration 0.066g L -1 .
[0021] Pipette 15.00mL of the liquid to be extracted, add 10mL of monooctyl phosphate and 2.0mL of kerosene as the extraction agent, and perform extraction. The contact time during extraction is 4 minutes, and the standing time is 3 minutes. Separate the acid leaching solution to be extracted vanadium, and then use 2mol L -1 The dilute sulfuric acid is used to back-extract the iron ions in the mixed extractant, which is used to extract another batch of acid leaching solution.
[0022] After extraction, the iron ion concentration in the vanadium solution was measured to be 0.051g L -1 , the concentration of iron ions decreased by...
Embodiment 2
[0024] Use concentrated sulfuric acid at 90°C to continuously leaching stone coal for 8 to 10 hours, filter out solid impurities to obtain an acid leaching solution, adjust the pH value of the acid leaching solution to 2.30±0.02 with ammonia water, and the concentration of iron ions at this time is 0.223g ·L -1 , vanadium ion concentration 0.074g L -1 .
[0025] Pipette 15.00 mL of the liquid to be extracted, add 10 mL of monobutyl phosphate, and 2.0 mL of kerosene as extraction agents for extraction. The contact time during extraction was 5 minutes, and the standing time was 4 minutes. The vanadium solution in the lower layer was separated, and 2mol·L -1 The dilute sulfuric acid will extract the iron ions in the mixed extractant.
[0026] After extraction, the iron ion concentration in the vanadium solution was measured to be 0.072g L -1 , the concentration of iron ions decreased by 67.7%, and the loss rate of vanadium was 22.6%.
Embodiment 3
[0028] Use concentrated sulfuric acid at 90°C to continuously leaching stone coal for 8-10 hours, filter out solid impurities to obtain an acid leaching solution, adjust the pH value of the acid leaching solution to 2.40±0.02 with ammonia water, and the concentration of iron ions at this time is 0.238g ·L -1 , vanadium ion concentration 0.079g L -1 .
[0029] Pipette 50.00 mL of the liquid to be extracted, add 15 mL of monohexyl phosphate and 2.5 mL of kerosene as extraction agents for extraction. The contact time during extraction is 4 minutes, and the standing time is 5 minutes. The vanadium solution in the lower layer was separated, and 2mol·L -1 The dilute sulfuric acid will extract the iron ions in the mixed extractant.
[0030] After extraction, the iron ion concentration in the vanadium solution was measured to be 0.078g L -1 , the concentration of iron ions decreased by 67.2%, and the loss rate of vanadium was 22.1%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More