Method for preparing high soda ash type copper carbonate by adopting duplex centrifugal film evaporator

A thin-film evaporator and copper carbonate technology, applied in chemical instruments and methods, copper compounds, inorganic chemistry, etc., can solve the problem that product fineness and precision cannot meet market requirements, pressure changes increase production difficulty, and affect the yield of basic copper carbonate. Yield and other issues, to achieve the effect of controllable production conditions, shorten the production cycle, and avoid the difficulty of cleaning

Active Publication Date: 2014-08-20
TAIXING SMELTING PLANT
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the commonly used method for producing basic copper carbonate uses copper sulfate, copper chloride or copper nitrate to synthesize basic copper carbonate with sodium carbonate or sodium bicarbonate in a dissolved state, and its disadvantages are long cycle, high energy consumption, and production The amount of waste water produced is large, the fineness and precision of the product cannot meet the market requirements, and the quality cannot be guaranteed; there are also methods for producing basic copper carbonate by the ammonia process, and the early method of producing basic copper carbonate by the ammonia process is mainly at room temperature Under strict compliance with Cu+(NH 4 ) 2 CO 3 +2NH 3 [o] →Cu(NH 3 ) 4 CO 3 This synthesis principle is carried out, because the volatility of ammonia, low temperature and other reasons cause the reaction time to be long, and it is difficult to obtain basic copper carbonate monomer. Although this method has been improved later, as the patent application number is 92109468.X " A high-efficiency process for producing basic copper carbonate or copper oxide. The process uses a mixture of heated copper material and ammonium bicarbonate solution. The whole process adopts a pressure-swing reaction, and then thermally decomposes at a temperature of 80 ° C to 100 ° C. Then, basic copper carbonate is obtained by washing and drying, but this method has high requirements on the pressure adjustment of the reaction. At the same time, most thermal decomposition devices use reactors to collect basic copper carbonate through coils. First, the pressure change increases the difficulty of production. Second, it is easy to accumulate and scale in the coil, which affects the yield of basic copper carbonate and also easily increases the impurities in the basic copper carbonate, especially iron, thereby affecting the quality of basic copper carbonate

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  • Method for preparing high soda ash type copper carbonate by adopting duplex centrifugal film evaporator
  • Method for preparing high soda ash type copper carbonate by adopting duplex centrifugal film evaporator

Examples

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Effect test

Embodiment 1

[0040] Using standard cathode copper, liquid ammonia, and carbon dioxide with a purity ≥ 99.9% as raw materials, the production process is as follows:

[0041] at 20m 3 pumped 15 meters into the concentrated ammonia water preparation tank with cooling coil 3 Deionized water, open the valve of the liquid ammonia steel cylinder, make the pressure of the liquid ammonia passing into the preparation tank be 0.2MPa, pass through the ammonia gas for 6 hours, prepare the concentrated ammonia water with a concentration of 135g / L, close the valve of the liquid ammonia steel cylinder; open the liquid ammonia located in the preparation tank The valve of the cooling water pipe in the medium but not connected with the concentrated ammonia water is fed with cooling water with a temperature of less than 15°C, and then the valve of the carbon dioxide steel cylinder is opened to control the pressure of the carbon dioxide introduced at 0.2MPa and the degree of carbonization at 80% to obtain carb...

Embodiment 2

[0045] Using standard cathode copper, liquid ammonia, and carbon dioxide with a purity ≥ 99.9% as raw materials, the production process is as follows:

[0046] at 20m 3 The strong ammonia water preparation tank with cooling coil, pumped into 15 meters 3 Deionized water, open the valve of the liquid ammonia steel cylinder, make the pressure of the liquid ammonia passing into the preparation tank be 0.15MPa, pass the ammonia gas for 7 hours, prepare the concentrated ammonia water with a concentration of 120g / L, close the valve of the liquid ammonia steel cylinder; open the liquid ammonia located in the preparation tank The valve of the cooling water pipe in the middle but not connected with the concentrated ammonia water is fed with cooling water with a temperature lower than 15°C, and then the valve of the carbon dioxide steel cylinder is opened, and the pressure of the carbon dioxide is controlled to be 0.15MPa, and the degree of carbonization is 100%, and the ammonium carbona...

Embodiment 3

[0050] Using standard cathode copper, liquid ammonia, and carbon dioxide with a purity ≥ 99.9% as raw materials, the production process is as follows:

[0051] at 20m 3 The strong ammonia water preparation tank with cooling coil, pumped into 15 meters 3 For deionized water, open the valve of the liquid ammonia steel cylinder, make the pressure of the liquid ammonia passing into the preparation tank be 0.1MPa, pass ammonia gas for 7 hours, and prepare concentrated ammonia water with a concentration of 85g / L, close the valve of the liquid ammonia steel cylinder; The valve of the cooling water pipe in the medium but not connected with the concentrated ammonia water is passed into the cooling water with a temperature of less than 15°C, and then the valve of the carbon dioxide cylinder is opened to control the pressure of the carbon dioxide introduced at 0.1MPa and the degree of carbonization at 140%. The amount of ammonium substance concentration is 3.5mol / L of carbonated ammonia...

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Abstract

The invention discloses a method for preparing high-purity alkaline copper carbonate by adopting a compound centrifugal thin-film evaporator. The method uses copper, liquid ammonia and high-purity carbon dioxide as raw materials, firstly prepares concentrated ammonia water, and then introduces high-purity carbon dioxide into the concentrated ammonia water The carbonized ammonia water is prepared, and the carbonized ammonia water is reacted with pure copper under a certain air pressure to obtain a copper-ammonia complex solution, and then evaporated, rotated and scraped by a compound centrifugal thin film evaporator to obtain a high-purity alkali type copper carbonate. The reaction speed shortens the production cycle, the product purity is higher, the production efficiency is greatly improved, the production cost is lower, the quality is significantly improved, and the product application is more extensive. Less, short reaction time, saving coal resources, greatly reducing production costs while more in line with environmental protection requirements.

Description

technical field [0001] The invention belongs to the field of production and application of copper carbonate, in particular to a method for preparing high-purity copper carbonate by using a compound centrifugal film evaporator. Background technique [0002] Basic copper carbonate is a widely used raw material in the chemical industry. It is used in the manufacture of various copper compounds in the inorganic industry, as a catalyst for organic synthesis in the organic industry, as an additive for copper ions in the electroplating industry, and in agriculture. It can be used as a preventive agent for smut, and can also be used as an insecticide for seeds. In animal husbandry, it can be used as an additive to copper in feed. It is also an important medicinal material. In addition, it is also used in pyrotechnics and pigment production. Substitutes for arsenic trioxide. At present, the commonly used method for producing basic copper carbonate uses copper sulfate, copper chlor...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01G3/00
Inventor 徐金章刘后传许明才
Owner TAIXING SMELTING PLANT
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