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Process for preparing high adsorbing active carbon by using petroleum coke as raw material

A high-adsorption, petroleum coke technology, applied in the field of activated carbon preparation, can solve the problems of unsatisfactory activation yield, high price, and high cost, and achieve the effects of stable product quality, reduced pollution, and reduced consumption

Inactive Publication Date: 2011-02-16
林建屏
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

U.S. Patent US5143889 uses mesophase pitch carbon microspheres as raw materials and uses potassium hydroxide (KOH) as an activator to obtain a specific surface area (BET) of 3000m 2 / g of activated carbon with ultra-high specific surface area, but because the mesophase pitch carbon microspheres are prepared by heat treatment of coal tar, the yield is only 10%, which greatly increases the cost of producing this activated carbon
Chinese patents CN93120925.0 and CN96123525.x both disclose a method for preparing activated carbon from pitch as a raw material. The activated carbon prepared by these methods has high specific surface area, good adsorption performance, low manufacturing cost, and low impurity ash content, etc. advantages, but its activation yield is still not ideal, and the high one is only about 25%.
In addition, there are also reports about using petroleum coke as a raw material to prepare activated carbon with an ultra-high specific surface area through chemical activation, but they are all directly mixed with alkaline solids, and the alkali-carbon ratio is as high as 10:1. Due to the high price of KOH (8000 yuan / ton), so the cost is too high and the pollution is serious

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Example 1: The raw petroleum coke (ash content 0.18%, volatile matter 7.02%, water content 0.13%, carbon content 92.60%) was crushed. Sieve to 81-100 mesh, and place in a vacuum dryer at 230°C for degassing. Prepare potassium hydroxide (KOH) solution or sodium hydroxide (NaOH) solution with a molar concentration of 0.2N, take 2.0g of 81-100 mesh petroleum coke, and immerse it in 50ml of potassium hydroxide (KOH) with a molar concentration of 0.2N In the solution, 2 drops of ethanol was added dropwise as a co-solvent, mixed evenly and then dried. In nitrogen (N 2 ) in an atmosphere of carbonization and activation (the temperature rise rate of the converter used as the activation equipment is selected as 20°C / min, the final temperature is less than 800°C (such as about 780°C), and the activation time is about 2 hours), after cooling to room temperature, take out the activation The product is washed successively with dilute hydrochloric acid and water to remove excess al...

Embodiment 2

[0019] Example 2: The raw petroleum coke (ash content 0.18%, volatile matter 7.02%, water content 0.13%, carbon content 92.60%) was crushed, sieved to 110-140 mesh, and degassed at 300°C. Prepare a potassium hydroxide (KOH) solution (or sodium hydroxide NaOH solution) with a molar concentration of 0.5N. Take 2.0g of 110-140mesh petroleum coke, immerse in 50ml of prepared alkaline medium potassium hydroxide (KOH) solution with a molar concentration of 0.5N, add 3 drops of ethanol dropwise, mix well and then dry. In nitrogen (N 2 ) in an atmosphere of carbonization and activation (heating rate of 20°C / min, final temperature of 798°C, and activation time of 2 hours), after cooling to room temperature, the activated product was taken out and washed with dilute hydrochloric acid and water successively to remove excess Alkaline medium and its products, after drying, about 0.84g of ultra-high specific surface area activated carbon is obtained, and its BET specific surface area is ab...

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Abstract

A method for preparing activated carbon with high adsorption activity by using petroleum coke as a raw material comprises the following steps: pulverizing the petroleum coke raw material into 81-150 mesh powder, and degassing in a 220-350 DEG C vacuum dryer to obtain a product A with a certain initial pore space; preparing an alkaline medium solution with a molar concentration of 0.2-0.5N, addingthe product A into the alkaline medium solution, adding a cosolvent, mixing uniformly, and allowing carbonization and alkaline activation treatment at 700-800 DEG C under inert gas atmosphere for 1-3hours to obtain a product B; and cooling the product B, washing and drying to obtain the final product. The inventive method has the following advantages that: the activated carbon prepared by using the method has rich micro-pores and has BET specific surface area of 2,500-3,000m<2> / g; the petroleum coke has a certain initial pore space and can mix and sufficiently contact with the alkaline medium solution, so as to reduce the consumption of the alkaline medium, reduce cost, reduce pollution, and unify reaction; and the activation rate and the yield are high, and the product quality is stable.

Description

(1) Technical field [0001] The invention belongs to a method for preparing activated carbon, in particular to a method for preparing (high specific surface area) highly adsorbable activated carbon by using petroleum coke as a raw material. (2) Background technology [0002] As a commonly used adsorbent, activated carbon is indispensable in industrial production and daily life. Traditional activated carbon is generally prepared from coal or various woods or plant husks. Due to the high ash content of impurities in coal, the activated carbon has high ash content of impurities, low specific surface area and unsatisfactory adsorption effect, which cannot meet the needs of food, The needs of important fields such as medicine, advanced environmental protection, chemical industry, and military affairs; wood chips, fruit shells, coconut shells, etc. are limited by the nature of the body and the resources of the origin of the production of activated carbon, so it is urgent to develop...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B31/12C01B31/08
Inventor 林建屏
Owner 林建屏
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