Method for producing feed grade zinc oxide through sodium chloride-ammonia combined leaching

A technology of combined leaching and sodium chloride, applied in the direction of zinc oxide/zinc hydroxide, etc., can solve the problems of economical reduction of zinc load in blast furnace, long process flow, weak permeability, etc., to improve zinc leaching speed and leaching rate, change Chemical composition and structure, the effect of accelerating zinc deposition rate

Active Publication Date: 2018-07-13
SICHUAN JUHONG TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the hygienic indicators such as lead, arsenic, cadmium and other heavy metals can be controlled by this method, the bulk density of the product is difficult to meet the requirements of the feed zinc oxide bulk density; the compatibility with other mixtures is quite different, and the mixing uniformity is not ideal
[0004] Patent CN 102627313 A (a wet production process of feed-grade active zinc oxide) utilizes ammonia water and ammonium bicarbonate in the ammonia immersion liquid as the carbonization precipitation agent of the acid immersion liquid, no additional use of ammonia water and ammonium bicarbonate, reducing the The ammonia distillation link greatly reduces the production cost, but the problem is that the recovery rate of neutralization is low, the ammonium sulfate solution of the neutralization solution is difficult to recycle and use, and ZnSO is easily produced 4 ·(NH 4 ) 2 SO 4 Double salt precipitation affects product quality
[0010] The disadvantage of patent CN 102826592 A (a method for producing active zinc oxide by using zinc-containing blast furnace ash and slag) is that it needs to be calcined to enrich high-content secondary oxygen powder, the process is long, and the sedimentation is compounded with zinc hydroxide and zinc carbonate. Precipitation in the form of salt, high calcination temperature (above 500°C), high energy consumption
[0012] Traditional ammonia leaching process generally adopts ammonia water and ammonium bicarbonate to cooperate to produce leaching solution, as

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0060] Raw material: soot ash 1# from a steel factory in Kunming, its composition is calculated by mass percentage (%):

[0061] 1#Zn8.6% Fe27.14% Pb0.85% Cd0.007% Fixed C28%

[0062] The method for preparing feed zinc oxide:

[0063] (a) Ball mill: take 500g of 1# soot, and grind it with a small ball mill until it passes through 180 mesh (80um);

[0064] (b) Leaching: the above material is leached with 1500ml sodium chloride-ammonia liquor-ammonium bicarbonate solution as a leaching agent; wherein, in the leaching agent, chloride ion c(Cl - )=0.58mol / L, NH 3 The molar concentration of c(NH 3 )=4.5mol / L, CO 3 2- The molar concentration of c(CO 3 2- )=0.7mol / L, three stages of leaching were carried out, and the leaching time of each stage was 2 hours. When leaching, wet ball milling was adopted, and the leaching time in the ball mill was guaranteed to be 50 minutes. After solid-liquid separation, the obtained zinc 40.21 grams of total zinc in the ammonia complex solutio...

Embodiment 2

[0069] Raw material: soot ash 2# from a steel plant in Hunan, the mass percentage (%) of its composition is:

[0070] Zn7.24% Fe 26.8% Pb0.57% S 0.47% SiO 2 5.57% Al 4.21%

[0071] The method for preparing feed zinc oxide:

[0072] (a) Ball mill: take 500g of soot ash 2#, and grind it with a small ball mill until all of it passes through 170 mesh (90um).

[0073] (b) Leaching: the above material is leached with 1500ml sodium chloride-ammonia liquor-ammonium bicarbonate solution as a leaching agent; wherein, in the leaching agent, chloride ion c(Cl - )=0.64mol / L, NH 3 The molar concentration of c(NH 3 )=5.8mol / L, CO 3 2- The molar concentration of c(CO 3 2- )=0.67mol / L, carry out three-stage stirring and leaching, and the leaching time of each stage is 2 hours, when leaching, adopt wet ball milling, and guarantee that the leaching time in the ball mill is 60 minutes, after solid-liquid separation, the obtained 33.95 grams of zinc (93.78% zinc recovery rate) in the zin...

Embodiment 3

[0078] Raw material: soot ash 3# from a steel factory in Northwest China, its composition is calculated by mass percentage:

[0079] Zn 11.3% Fe 30.53% Pb 0.48% C 25.28% SiO 2 5.34% MgO 1.56%

[0080] The method for preparing feed grade zinc oxide:

[0081] (a) Ball mill: take 1000g of soot ash 3#, and grind it with a small ball mill until all of it passes through 175 mesh (86um).

[0082] (b) Leaching: the above material is leached with 3000ml sodium chloride-ammonia liquor-ammonium bicarbonate solution as a leaching agent; wherein, in the leaching agent, chloride ion c(Cl - )=0.66mol / L, NH 3 The molar concentration of c(NH 3 )=5.6mol / L, CO 3 2- The molar concentration of c(CO 3 2- )=0.72mol / L, carry out three stages of stirring and leaching, and the leaching time of each stage is 2 hours. When leaching, adopt wet ball milling, and ensure that the leaching time in the ball mill is 60 minutes. After solid-liquid separation, the obtained 104.46 grams of total zinc in ...

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Abstract

The invention discloses a method for producing feed grade zinc oxide through sodium chloride-ammonia combined leaching. The method comprises the following steps: leaching smoke dust of a steel mill, purification and dust removal, distilling ammonia and depositing zinc and drying and calcining, wherein when the smoke dust of the steel mill is leached, ammonium hydroxide, ammonium bicarbonate and sodium chloride are taken as leaching agents. The method has the advantages a sodium chloride solution is added to leaching liquid, the zinc leaching speed and leaching rate in the smoke dust are improved, the fact that the leaching rate of impurities, such as iron, is extremely low can be further guaranteed, the zinc depositing speed during ammonia seperation is further accelerated, the chemical components and structure of a product are changed, a solution can be completely used for performing circulation ammonia absorption leaching utilization after ammonia separating and zinc depositing, andthe cost is saved; an adopted technology changes the phase components of a product intermediate, low calcination temperature can be adopted, a feed zinc oxide product with the content of high bulk density being capable of reaching greater than 99.0 percent, and the method has excellent economic benefit.

Description

technical field [0001] The invention belongs to the field of zinc oxide production, in particular to a method for producing feed-grade zinc oxide through sodium chloride-ammonia combined leaching. Background technique [0002] Feed zinc oxide is used as an additive in feed. Compared with other zinc sources, it has the following characteristics: good stability in feed, no caking, no denaturation, convenient for feed premix processing and long-term storage; little effect on vitamins in feed . It has special requirements on indicators, such as lead, arsenic, cadmium and other heavy metal indicators are strictly controlled, and its physical data such as bulk density also have special requirements. Its function is to prevent diarrhea in weaned piglets, promote digestion, increase growth rate and reduce mortality. If the mixture is uneven, the local zinc will exceed the standard, which will bring toxicity to animals. In order to enhance the mixing uniformity of the feed, the ph...

Claims

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Application Information

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IPC IPC(8): C01G9/02
CPCC01G9/02C01P2006/11C01P2006/80
Inventor 王吉白李时春李旸阳浦仕福
Owner SICHUAN JUHONG TECH
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