Method for preparing high-activity electroplating grade copper oxide from basic cupric carbonate

A technology of electroplating grade copper oxide and copper carbonate, applied in the direction of copper oxide/copper hydroxide

Inactive Publication Date: 2013-05-15
TAIXING SMELTING PLANT
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Regarding the production process of copper oxide, it is also involved in some invention patents disclosed at present. The application number is 01127175.2, which uses copper sulfate and copper material as raw materials, undergoes low-temperature oxidation at 80-85°C, obtains copper sulfate through crystallization, and then mixes it with Sodium hydroxide reaction, and then through ball milling, pressure filtration, washing, drying, and pulverization to obtain active copper oxide. Waste water; Application number is the technique that 200710076208.1 discloses to produce copper oxide through distilling ammonia with alkaline etching waste liquid, owing to be to make by distilling ammonia for a long time under high temperature, strong alkali state with alkaline etching waste liquid, so copper oxide activity is relatively Low; the application number is 200710071896.2, which discloses the reaction of copper nitrate and sodium hydroxide through pressure filtration, drying, and roasting to produce copper oxide, which will produce nitrogen dioxide or nitrogen monoxide waste gas, which will cause certain pollution to the environment; application number is 200810067243.1 The production process of synthesizing basic copper chloride as a precursor, and then reacting with sodium hydroxide to produce monoclinic copper oxide, but its activity has not been verified experimentally
At present, copper oxide for horizontal electroplating is also prepared from basic copper carbonate as raw material, but first, basic copper carbonate is mostly obtained by traditional technology, and the content of impurities such as iron and lead is high. Second, most manufacturers use pusher kiln calcining equipment for calcination. Basic copper carbonate prepares electroplating-grade copper oxide. This method has the following problems: (1) Due to the uneven temperature distribution in the kiln, the physical properties of the reaction material are not uniform enough, and the low-temperature part of the basic copper carbonate has not enough fire-through content, while the high-temperature part is oxidized. The copper has been burnt to death and loses its activity; (2) The slag from the charging sagger brings impurities such as silicon, aluminum, calcium and other contaminated products into the material, making the chemical composition of the electroplating grade copper oxide unable to meet the target requirements; (3) Because the material is fixed Bed, uneven temperature distribution, long production time and high energy consumption; (4) manual operation, labor-intensive, can not be automated

Method used

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  • Method for preparing high-activity electroplating grade copper oxide from basic cupric carbonate
  • Method for preparing high-activity electroplating grade copper oxide from basic cupric carbonate
  • Method for preparing high-activity electroplating grade copper oxide from basic cupric carbonate

Examples

Experimental program
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Effect test

Embodiment 1

[0053] at 20m 3 pumped 15 meters into the concentrated ammonia water preparation tank with cooling coil 3Deionized 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 carbonic acid The amount concentration of ammonium substance is that the carbonated ammonia water of 3.18mol / L is packed into the storage container; In the co...

Embodiment 2

[0059] 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 carbonate substance is obtained. The quantity concentration is 3.53mol / L the carbonized ammonia water puts into the storage container; Puts 62.5×10 3 mol stand...

Embodiment 3

[0065] 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 water into the storage container; 62.5 × 10 3 mol standard cathode copper plate, pumped into 3.5m3 containing 12.25×10 3 The carbonized ammonia water ...

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Abstract

The invention discloses a method for preparing high-activity electroplating grade copper oxide from basic cupric carbonate. According to the method, pure copper, liquid nitrogen and high-purity carbon dioxide are taken as materials to prepare the high-purity basic cupric carbonate through a centrifugal film evaporator or a scraper reaction kettle; the problem of impurities such as chlorine which may be caused by production of the basic cupric carbonate material by the traditional method is avoided; the purity of the basic cupric carbonate is improved; the high-purity low-chorine electroplating grade copper oxide is burnt from the high-purity basic cupric carbonate through a rotary kiln; the defects of inactivation, a plurality of impurities, large labor intensity, un-continuous production, long period, high energy consumption, large cost and the like due to the fact that the basic cupric carbonate at the low-temperature part is not burnt thoroughly and the content is not enough when a pushed slab kiln statically burns while copper oxide at the high-temperature part is burnt to death are overcome; the product activity is ensured; and the method is high in product quality, less in energy consumption, small in cost and more environment-friendly.

Description

technical field [0001] The invention belongs to the field of copper oxide production, in particular to a method for preparing high-activity electroplating grade copper oxide from basic copper carbonate. Background technique [0002] In the PCB manufacturing process, the traditional electroplating process uses a copper plate as the anode plate and supplements the copper source. Due to the complex shape of the electronic components, there are holes, concave-convex surfaces and other shapes. In the holes, the electroplating solution cannot penetrate, so the plating Less than copper, the protruding part has a high current density and a thick coating, while the concave part has a low current density and a thin coating, resulting in unqualified products. [0003] At present, the horizontal electroplating process is common in the PCB manufacturing industry in the market. This process overcomes the shortcomings of the traditional process, but this process must add high-purity, low-c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G3/02
Inventor 徐金章刘后传许明才
Owner TAIXING SMELTING PLANT
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