Chemical extraction and recovery method for carbon black after waste rubber decomposition

A chemical and waste rubber technology, which is applied in solid solvent extraction, nickel sulfate, alkali metal silicate, etc., can solve the problems of resource waste, industry development restrictions of waste rubber cracking and recycling, increased processing costs and environmental burdens, etc. , to achieve the effect of improving the quality

Inactive Publication Date: 2018-04-24
张瑞永
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  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In order to remove sulfur dioxide, the air pollution factor, the easiest way is to wash and intercept the burned sulfur dioxide with water in the scrubber. Sulfur dioxide is easily dissolved in water in the scrubber to form a sulfuric acid solution. The sulfuric acid solution needs to be neutralized with lye. It can be discharged or entered into the wastewater treatment system for further treatment, resulting in waste of resources and increased treatment costs and environmental burdens
[0005] The carbon black in the rubber component is the main recycling target in the current technology. Carbon black is the reinforcing material of the rubber mixture. Due to its excellent stability, carbon black can be recycled and reused in theory. However, due to the rubber formula It is necessary to add other metal and non-metal oxides or compounds to meet the basic specifications used in general commercial use. Such substances cannot be separated from solid carbon black in the waste rubber cracking process, or because of high temperature cracking, Part of the substance also participates in the chemical reaction, resulting in additional ash, the so-called carbon black ash
Therefore, the purity of carbon black is not good, generally containing about 10-20% ash, which affects the reinforcing effect of recycled carbon black added to rubber, greatly reducing the applicability and marketability of recycled carbon black in rubber, It also leads to great restrictions on the development of waste rubber cracking and recycling industry
[0006] The current technology mainly uses acidic solution and chelating agent to carry out pickling process on carbon black. The ash of carbon black is chemically reacted with acidic solution, and the metal ion in the ash of carbon black is chelated and separated by chelating agent. The main technology to reduce the ash content of carbon black, however, because additional chelating agents are added, it also increases the processing cost and the burden on the environment

Method used

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  • Chemical extraction and recovery method for carbon black after waste rubber decomposition

Examples

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Comparison scheme
Effect test

Embodiment 1

[0074] Provide 50 grams of pyrolysis solids, measuring about 15.45% ash, which is ground recovered carbon black, which is obtained from recycled waste rubber through a general cracking process.

[0075] An acid solution is provided, which is to provide 1 liter of pure water and add about 10 grams of concentrated sulfuric acid to prepare a 0.1N sulfuric acid solution.

[0076] Slowly place the sulfuric acid solution (acid solution) and the recovered carbon black (cracked solids) into the stirring device, so that the recovered carbon black is completely immersed in the sulfuric acid solution, and continue to stir for 2 hours, and gradually heat up to 70°C at room temperature (section a stirring process) to generate the first mixed solution.

[0077] Stirring is stopped, and the first mixed solution is separated into a first precipitate and a first solution through an extraction process, a precipitation process, and a filtration process (a first separation process).

[0078] Was...

Embodiment 2

[0087] Provide 100 grams of cracked solids, measuring about 15.45% ash, which is ground recovered carbon black, which is obtained from recycled waste rubber through a general cracking process.

[0088] An acid solution is provided, which is to provide 1 liter of pure water and add about 100 grams of concentrated sulfuric acid to prepare a 1N sulfuric acid solution.

[0089] Slowly place the sulfuric acid solution (acid solution) and recovered carbon black (cracked solids) into the stirring device, so that the recovered carbon black is completely immersed in the sulfuric acid solution, and continue to stir for 1 hour, and gradually heat up to 80°C at room temperature (section a stirring process) to generate the first mixed solution.

[0090] Stirring is stopped, and the first mixed solution is separated into a first precipitate and a first solution through an extraction process, a precipitation process, and a filtration process (a first separation process).

[0091] Wash the f...

Embodiment 3

[0100] Provide 50 grams of cracked solids, measuring about 15.45% ash, which is ground recovered carbon black, which is obtained from recycled waste rubber through a general cracking process.

[0101] Provide an acid solution, use the waste reduction equipment washing tower in the cracking process, pass the sulfur dioxide produced in the process through the washing tower, and hydrolyze the sulfur dioxide and water into a sulfuric acid solution, and collect the recovered sulfuric acid solution into the acidification tank. Sulfuric acid solution, the recovered sulfuric acid solution and concentrated sulfuric acid are prepared into 1N, 1 liter sulfuric acid solution.

[0102] Slowly place the sulfuric acid solution (acid solution) and the recovered carbon black (cracked solid) into the stirring device, so that the recovered carbon black is completely immersed in the sulfuric acid solution, and continue to stir for 3 hours, and gradually heat up to 90°C at room temperature (section...

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Abstract

The invention provides a chemical extraction and recovery method for carbon black after waste rubber decomposition. The chemical extraction and recovery method at least comprises following steps: providing a decomposed solid which is obtained through waste rubber decomposition; providing an acid solution, placing the acid solution and the decomposed solid in a stirring device, carrying out a firststirring process, and generating a first mixed solution; separating the first mixed solution into a first solution and a first precipitate through a first separation process, and obtaining a first metallic compound from the first solution through a first dehydration process; providing an alkaline solution, placing the alkaline solution and the first precipitate in the stirring device, carrying out a second stirring process, and generating a second mixed solution; separating the second mixed solution into a second solution and a second precipitate through a second separation process, and obtaining a second metallic compound from the second solution through a second dehydration process; and obtaining carbon black from the second precipitate through a third dehydration process.

Description

technical field [0001] The invention relates to a method for extracting and recovering chemicals from carbon black after waste rubber cracking, in particular to recycling sulfur dioxide produced in waste rubber cracking process, reusing high-value chemicals, and improving the quality of carbon black. The extraction and recovery method of carbon black. Background technique [0002] Nowadays, people around the world communicate frequently, and as a result of frequent exchanges, people from all over the world continue to move to different places, which greatly increases the demand for transportation tools. No matter taking an airplane or a vehicle, tires are required, and the usage of tires is also greatly increased. The increase in the use of tires increases the number of tires that need to be replaced due to wear and tear, and the tires are rubber products. Therefore, the recovery and reuse of waste rubber has become an important issue. [0003] The main technology for recyc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D11/02C01G9/06C01G53/10C01G51/10C01F11/46C01B33/32C09C1/48
CPCB01D11/02C01B33/32C01F11/46C01G9/06C01G51/10C01G53/10C09C1/482C09C1/487
Inventor 张瑞永
Owner 张瑞永
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