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Method for preparing activated carbon adsorbent from coal-oil corefining residue

A technology for preparing activated carbon from kerosene co-refining residues, applied in chemical instruments and methods, other chemical processes, inorganic chemistry, etc., can solve the problems such as the technical report of activated carbon adsorbent that has not yet been reported, the high moisture content of passion fruit peel, and the waste of biological resources. Achieve the effect of optimizing pore structure distribution, good surface adsorption space structure, and improving adsorption performance

Active Publication Date: 2021-02-26
THE NORTHWEST RES INST OF CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In the whole passion fruit fresh fruit, the pericarp accounts for about 50% to 55%. However, the current domestic development of passion fruit products is mainly concentrated in the processing of pulp beverages. This not only causes a waste of biological resources, but also pollutes the environment.
[0005] At present, there is no technical report on the preparation of activated carbon adsorbent from kerosene co-refining residue and passion fruit peel

Method used

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  • Method for preparing activated carbon adsorbent from coal-oil corefining residue
  • Method for preparing activated carbon adsorbent from coal-oil corefining residue

Examples

Experimental program
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Effect test

Embodiment 1

[0033] This embodiment includes the following steps:

[0034]Step 1, crushing the kerosene co-refining residue into kerosene co-refining residue particles with a particle size of 1 mm to 3 mm, then blending dried passion fruit peel particles with a particle size of 1 mm to 3 mm according to a mass ratio of 5:1 for conditioning treatment, and then According to the impregnation ratio of 1:3, place it in a KOH solution with a mass concentration of 50%, stir and impregnate it at a speed of 200r / min at room temperature for 2h to obtain a mixture;

[0035] Step 2. Under a nitrogen atmosphere, the mixture obtained in Step 1 was activated once for 30 minutes with a 1000W microwave, then washed with distilled water to neutrality and dried to obtain the activated product I;

[0036] Step 3: crushing part of the activated product I obtained in step 2 until the particle size does not exceed 150 μm, and then performing secondary activation for 15 minutes with 800W microwave under a nitroge...

Embodiment 2

[0043] This embodiment includes the following steps:

[0044] Step 1, crushing the kerosene co-refining residue into kerosene co-refining residue particles with a particle size of 1 mm to 3 mm, then blending dried passion fruit peel particles with a particle size of 1 mm to 3 mm according to a mass ratio of 1:1 for conditioning treatment, and then According to the impregnation ratio of 1:1, it is placed in KOH and K with a mass concentration of 20%. 2 CO 3 In the mixed solution, stir and impregnate at room temperature at a speed of 200r / min for 3h to obtain a mixture; the KOH and K 2 CO 3 KOH and K in the mixed solution 2 CO 3 The mass ratio is 2:1;

[0045] Step 2. Under a nitrogen atmosphere, the mixture obtained in Step 1 was activated once for 60 minutes with a 100W microwave, and then washed with distilled water to neutrality and dried to obtain the activated product I;

[0046] Step 3: crushing part of the activated product I obtained in step 2 until the particle s...

Embodiment 3

[0053] This embodiment includes the following steps:

[0054] Step 1, crushing the kerosene co-refining residue into kerosene co-refining residue particles with a particle size of 1 mm to 3 mm, then blending dried passion fruit peel particles with a particle size of 1 mm to 3 mm according to a mass ratio of 3:1 for conditioning treatment, and then According to the impregnation ratio of 1:2, it is placed in a NaOH solution with a mass concentration of 35%, and stirred and impregnated at a speed of 300r / min at room temperature for 1.5h to obtain a mixture;

[0055] Step 2. Under a nitrogen atmosphere, the mixture obtained in Step 1 was activated once with 600W microwave for 45 minutes, then washed with distilled water to neutrality and dried to obtain the activated product I;

[0056] Step 3: crushing part of the activated product I obtained in step 2 until the particle size does not exceed 150 μm, and then performing secondary activation with 100W microwave for 5 minutes under ...

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Abstract

The invention discloses a method for preparing an activated carbon adsorbent from coal-oil corefining residue, which comprises the following steps: 1, blending coal-oil corefining residue particles with passion fruit peel particles, carrying out quenching and tempering treatment, and dipping in an activator solution to obtain a mixture; 2, performing primary activation on the mixture to obtain anactivated product I; 3, crushing the activation product I, and carrying out secondary activation to obtain an activation product II; 4, mixing, kneading and granulating the activated product I, the activated product II and bentonite so as to obtain prefabricated particles, and then spraying a surfactant aqueous solution to obtain the activated carbon adsorbent. According to the invention, waste passion fruit peel particles are adopted for loosening and granulating tempering treatment, the self-adhesion property and adhesion property of the coal-oil corefining residue residue particles in the stirring and activating process are reduced; then a graded pore structure with different pore size distribution is obtained in combination with two times of activating and forming processes, so that pore structure distribution is further optimized, the adsorption performance of the activated carbon adsorbent is improved, and the recovery treatment of the waste is realized.

Description

technical field [0001] The invention belongs to the technical field of residue treatment and utilization, and in particular relates to a method for preparing an activated carbon adsorbent from kerosene co-refining residue. Background technique [0002] The kerosene co-refining technology is to mix coal slurry and heavy and low-quality oil in a certain proportion, and then under certain pressure and temperature and using a certain catalyst, the mixed oil coal slurry passes through the reactor at one time and simultaneously hydrocracks into light and medium oil. and a small amount of hydrocarbon gas technology. This process technology has the advantages of high oil yield, low hydrogen consumption, and high hydrogen utilization rate, and realizes the clean utilization of coal and the lightening of heavy and inferior oil. [0003] Kerosene co-refining technology is transformed to produce 5% to 30% residue, which is rich in unconverted coal, heavy low-quality oil and inorganic m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B32/33C01B32/324C01B32/348C01B32/384B01J20/20B01J20/30
CPCC01B32/33C01B32/324C01B32/348C01B32/384B01J20/20B01J2220/4887Y02A50/20
Inventor 谢欣馨韦孙昌徐宏伟袁善录贺根良戴爱军郑亚兰林益安朱春鹏杜彦学王锦
Owner THE NORTHWEST RES INST OF CHEM IND