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Method for lixiviating molybdenum from roasted molybdenite

A molybdenum calcining and leaching technology, applied in the field of hydrometallurgy, can solve the problems of affecting the leaching rate of molybdenum, cumbersome process methods for recovering molybdenum, troublesome treatment of ammonia leaching slag, etc.

Active Publication Date: 2013-11-27
JINDUICHENG MOLYBDENUM CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, this traditional ammonia leaching method has the following problems: 1. Molybdenum calcine not only contains molybdenum trioxide, but also a small amount of gangue minerals such as calcium molybdate, magnesium molybdate, iron molybdate, etc., wherein calcium molybdate and molybdate Magnesium is insoluble or hardly soluble in ammonia water, and after ammonia leaching, it enters the ammonia leaching residue, causing a large loss of molybdenum and affecting the leaching rate of molybdenum; 2. Ferric molybdate in molybdenum calcine meets alkali in the ammonia leaching process to form hydrogen oxidation Iron colloid, which wraps on the surface of molybdenum calcine particles in the form of a film, hinders the dissolution of molybdenum trioxide in molybdenum calcine and forms molybdenum trioxide aggregates
Calculated according to the existing water washing-ammonia leaching process, for every 100 tons of ammonium molybdate produced, 2.2 to 3.3 tons of molybdenum metal will be lost due to non-leaching, and the lost molybdenum exists in the ammonia leaching residue, while the ammonia leaching residue The treatment is cumbersome, and the process of recovering molybdenum is cumbersome, so it is necessary to increase the leaching rate of molybdenum calcined sand and reduce the loss of molybdenum in the slag

Method used

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  • Method for lixiviating molybdenum from roasted molybdenite
  • Method for lixiviating molybdenum from roasted molybdenite
  • Method for lixiviating molybdenum from roasted molybdenite

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Embodiment 1

[0024] The method for leaching molybdenum from molybdenum calcine in the present embodiment comprises the following steps:

[0025] Step 1, after molybdenum calcined sand, ammonium carbonate and deionized water are mixed uniformly in a mass ratio of 1:0.75:2.5, the temperature is stirred at 80°C for 60 minutes to obtain a suspension; the molybdenum calcined sand contains molybdenum The mass percentage content is 63%;

[0026] Step 2, filtering the suspension described in step 1 to obtain filter cake and filtrate;

[0027] Step 3, adopting the ammoniacal liquor that mass percent concentration is 26% to wash the filter cake described in step 2, then the ammoniacal liquor after washing is mixed with the filtrate described in step 2, obtains mixed solution; The consumption of described ammoniacal liquor is molybdenum 0.9 times the quality of calcined sand, and the number of washings is 2 times;

[0028] Step 4, using liquid ammonia or ammonia water with a mass percentage concent...

Embodiment 2

[0034] The method for leaching molybdenum from molybdenum calcine in the present embodiment comprises the following steps:

[0035] Step 1, after molybdenum calcined sand, ammonium carbonate and deionized water are mixed uniformly by mass ratio 1:0.82:3, stir 70min under the condition that temperature is 70 ℃, obtain suspension liquid; The molybdenum in described molybdenum calcined sand The mass percentage content is 63%;

[0036] Step 2, filtering the suspension described in step 1 to obtain filter cake and filtrate;

[0037] Step 3, adopting the ammoniacal liquor that mass percentage concentration is 28% to wash the filter cake described in step 2, then the ammoniacal liquor after washing is mixed with the filtrate described in step 2, obtains mixed solution; The consumption of described ammoniacal liquor is molybdenum 0.8 times the quality of calcined sand, and the number of washings is 1 time;

[0038] Step 4: Adjust the pH value of the mixed solution described in step ...

Embodiment 3

[0044] The method for leaching molybdenum from molybdenum calcine in the present embodiment comprises the following steps:

[0045] Step 1, after molybdenum calcined sand, ammonium carbonate and deionized water are mixed uniformly by mass ratio 1:0.66:3, stir 40min under the condition that temperature is 90 ℃, obtain suspension liquid; The molybdenum in described molybdenum calcined sand The mass percentage content is 62.4%;

[0046] Step 2, filtering the suspension described in step 1 to obtain filter cake and filtrate;

[0047] Step 3, adopting the ammoniacal liquor that mass percentage concentration is 25% to wash the filter cake described in step 2, then the ammoniacal liquor after washing is mixed with the filtrate described in step 2, obtains mixed solution; The consumption of described ammoniacal liquor is molybdenum 0.6 times the quality of calcined sand, and the number of washings is 2 times;

[0048] Step 4: Adjust the pH value of the mixed solution described in st...

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Abstract

The invention discloses a method for lixiviating molybdenum from roasted molybdenite. The method comprises the following steps of: 1, uniformly mixing the roasted molybdenite, ammonium carbonate and deionized water at a certain mass ratio, and then stirring for 40-70 minutes under the condition that the temperature is 70-90 DEG C to obtain a turbid liquid; 2, filtering to obtain a filter cake and filter liquor; 3, washing the filter cake by adopting ammonia water, then uniformly mixing the washed ammonia water with the filter liquor to obtain a mixed liquor; 4, regulating the pH value of the mixed liquor to 8.0-8.5, uniformly stirring, then carrying out sedimentation treatment, and taking a supernatant to obtain molybdenum lixivium. The process disclosed by the invention is simple, easy to operate, high in repeatability and suitable for large-scale industrial production, adopts the ammonium carbonate as a lixiviant, and can be used for greatly reducing the sludging ratio and the molybdenum content of dregs by regulating and optimizing the lixiviating process, and achieving the molybdenum lixiviating rate as high as more than 98%.

Description

technical field [0001] The invention belongs to the technical field of hydrometallurgy, in particular to a method for leaching molybdenum from molybdenum calcined sand. Background technique [0002] Molybdenum calcined sand, also known as industrial molybdenum oxide, is an important chemical raw material, which is roasted and smelted from molybdenum concentrate. Molybdenum calcined sand is used to prepare ammonium molybdate. Ammonium molybdate is an important chemical product, mainly used in powder metallurgy and electronics industry, and is the basic raw material for making molybdenum powder. In addition, molybdenum calcine can also be used as a catalyst, smoke suppression and flame retardant, pigment, etc. in the petroleum industry. [0003] In the process of using molybdenum calcine to prepare ammonium molybdate, ammonia leaching process is generally used to leach molybdenum from molybdenum calcine, so that molybdenum trioxide, the main component of molybdenum calcine, i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/14C22B34/34
CPCY02P10/20
Inventor 唐军利
Owner JINDUICHENG MOLYBDENUM CO LTD
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