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Medium-temperature hydrophobic decarburization adsorbent and preparation method thereof

An adsorbent and medium-temperature technology, applied in the field of clean energy, can solve problems such as high temperature of mixed gas and decreased decarbonization ability

Active Publication Date: 2021-12-28
TSINGHUA UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, when activated carbon is used as an adsorbent for dry decarbonization, due to the capillary phenomenon on the surface of activated carbon, a large amount of water in the environment is adsorbed on the surface of the activated carbon, which greatly reduces the decarbonization ability during the adsorption process; such as coal to hydrogen and hydrocarbon In the similar reforming hydrogen production industry, the temperature of the mixed gas before purification is relatively high (200~350 o C) and contains water vapor

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  • Medium-temperature hydrophobic decarburization adsorbent and preparation method thereof
  • Medium-temperature hydrophobic decarburization adsorbent and preparation method thereof
  • Medium-temperature hydrophobic decarburization adsorbent and preparation method thereof

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preparation example Construction

[0043] The invention provides a method for preparing a medium-temperature hydrophobic decarburization adsorbent, comprising the following steps:

[0044] a) Mix carbon source, nitrogen source and organic solvent and dry to obtain a primary precursor;

[0045] b) carbonizing the primary precursor to obtain a carbonized product;

[0046] c) mixing the carbonized product with zinc chloride and an organic solvent and then drying to obtain a secondary precursor;

[0047] d) thermally activating the secondary precursor to obtain a medium-temperature hydrophobic decarburization adsorbent;

[0048] The carbon source is anthracite and medium temperature coal tar pitch.

[0049] Regarding step a): mixing carbon source, nitrogen source and organic solvent and then drying to obtain a primary precursor.

[0050] In the present invention, the carbon source is anthracite and medium temperature coal tar pitch.

[0051]The anthracite is a coal raw material with the most balanced distributi...

Embodiment 1

[0081] Embodiment 1: preparation U 15 A 9 C 1 Z 10 -700 nitrogen doped hydrophobic activated carbon

[0082] S1. Preparation of primary precursor

[0083] Weigh 10 parts of CTP and dissolve in 200 parts of tetrahydrofuran-ethanol mixed solvent (the volume fraction of tetrahydrofuran in the mixed solvent is 25%), then weigh 180 parts of urea and dissolve in the above solvent. After that, weigh 90 parts of anthracite, disperse it in the above system, heat it in a constant temperature water bath to 65°C, stir and mix at a speed of 150 rpm, and volatilize the solvent at the same time. Transfer to an alumina quartz boat, and air-dry at 70°C for 5 hours to obtain a primary precursor, denoted as [A] 9 [C] 1 [U] 15 .

[0084] Among them, the carbon content of anthracite is recorded as 90%, and the carbon content of CTP is recorded as 75%. The nitrogen content of urea is recorded as 52%. It is required that the carbon-nitrogen ratio in the precursor reaches 10:15, so 100 part...

Embodiment 2

[0091] Example 2: Preparation of M 15 A 9 C 1 Z 10 -700 nitrogen doped hydrophobic activated carbon

[0092] 1. Sample preparation:

[0093] S1. Preparation of primary precursor

[0094] Weigh 10 parts of CTP and dissolve in 200 parts of tetrahydrofuran-ethanol mixed solvent (the volume fraction of tetrahydrofuran in the mixed solvent is 25%), then weigh 150 parts of melamine, and add melamine into the dispersion system at a rate of 6 parts / min. until a non-settling emulsion dispersion is formed. Heat the dispersion system in a constant temperature water bath to 65°C, stir and mix at a speed of 150 rpm, and at the same time volatilize the solvent. When it becomes a viscous paste, transfer it to an alumina quartz boat, and air-dry it at 100°C for 5 hours to obtain a Grade precursor, denoted as [A] 9 [C] 1 [M] 15 .

[0095] S2, carbonization treatment

[0096] The resulting primary precursor [A] 9 [C] 1 [M] 15 Placed in a tube furnace, fed high-purity nitrogen with...

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Abstract

The invention provides a medium-temperature hydrophobic decarburization adsorbent and a preparation method thereof. The preparation method of the medium-temperature hydrophobic decarburization adsorbent comprises the steps of a) mixing a carbon source, a nitrogen source and an organic solvent, and drying to obtain a primary precursor; b) carbonizing the primary precursor to obtain a carbonized product; c) mixing the carbonized product with zinc chloride and an organic solvent, and drying to obtain a secondary precursor; and d) carrying out thermal activation treatment on the secondary precursor to obtain the medium-temperature hydrophobic decarburization adsorbent, wherein the carbon source is anthracite and medium-temperature coal pitch. The medium-temperature hydrophobic decarburization adsorbent prepared by the method not only has a larger specific surface area and stronger decarburization adsorption capacity, but also has better hydrophobic capacity and keeps better decarburization adsorption capacity under a medium-temperature condition.

Description

technical field [0001] The invention relates to the technical field of clean energy, in particular to a medium-temperature hydrophobic decarbonization adsorbent and a preparation method thereof. Background technique [0002] In industrial production and daily life, carbon dioxide (CO 2 ) The generation and emission of gas is inevitable. Such gases will cause the greenhouse effect of the atmosphere and destroy the ecological environment of the earth. In the coal-to-hydrogen and hydrocarbon reforming hydrogen-to-hydrogen industries, CO 2 and other carbon-containing impurity gas components are removed. Traditional solution absorption and adsorption methods are used in the temperature range below 100°C, resulting in waste of energy, high cost, and secondary pollution. Therefore, dry decarbonization has better prospects in terms of energy saving, emission reduction and cost reduction. [0003] In the dry decarbonization process, the synthesis and application of adsorbents are...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/20B01D53/02B01J20/30
CPCB01J20/20B01D53/02B01J20/0244B01J20/0259B01D2257/504Y02C20/40
Inventor 史翊翔李爽陈优蔡宁生
Owner TSINGHUA UNIV