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Preparation method of mercury removal adsorbent based on activated coke and product

An adsorbent and activated coke technology, applied in the field of preparation of mercury removal adsorbents, can solve the problems of poor product quality consistency, uneven loading, low sulfur loading rate, etc., achieve high product consistency, solve low sulfur loading rate, The effect of increasing the sulfur loading rate

Pending Publication Date: 2021-04-13
BEIJING SPC ENVIRONMENT PROTECTION TECH
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  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] For this reason, the present invention provides a preparation method and product of a mercury removal adsorbent based on activated coke, in order to at least partially solve the problem of low sulfur loading rate, uneven loading, and poor product quality consistency in the existing preparation method of mercury removal adsorbent. technical issues

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  • Preparation method of mercury removal adsorbent based on activated coke and product

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preparation example Construction

[0025] In a specific embodiment, the preparation method of the activated coke-based mercury removal adsorbent provided by the present invention uses small-particle activated coke as raw material, supplemented with a certain proportion of sulfur, and adopts the method of rotating and heating in a closed reactor Prepare. Such as figure 1 As shown, it specifically includes the following steps:

[0026] S1: Mix active coke with a preset index and sulfur with a preset particle size according to a preset ratio to obtain a mixture; specifically, the active coke is unshaped granular coal-based active coke, and the preset index is a particle size of 3mm ~8mm, specific surface area 300m2 / g~600m2 / g, ignition point ≥ 420°C, preset particle size of the sulfur is 40 mesh to 200 mesh, preset ratio of active coke and sulfur in the mixture The ratio is a preset mass ratio, and the preset mass ratio is active coke:sulfur=100:3˜100:20.

[0027] That is to say, in the preparation stage of raw ...

Embodiment 1

[0039] First of all, the coal quality amorphous granular activated coke selected in the test has a particle size of 2mm-3mm, a specific surface area of ​​550m2 / g, an ignition point of 440°C, and is dried at 105°C for 2 hours before use; the sulfur is crushed to 60-160 mesh. Weigh 100 grams of screened active coke in proportion, and then weigh 10 grams of sulfur (according to the sulfur-to-carbon ratio of 10%), and manually mix and stir in a glass container.

[0040] Transfer the primary mixed active coke and sulfur samples into the special closed reactor for the test, fully tighten it and then shake it gently for secondary mixing, then place the closed reactor in the tubular resistance furnace, and connect the rotating system at both ends .

[0041] Set the test parameters related to co-thermal modification load. In this example, set the heating rate to 10°C / min, and keep it at the final reaction temperature of 550°C for 2 hours. The reactor rotation frequency is 15Hz. Stop th...

Embodiment 2

[0044] First of all, the coal quality amorphous granular activated coke selected in the test has a particle size of 5mm-6mm, a specific surface area of ​​535m2 / g, an ignition point of 440°C, and is dried at 105°C for 2 hours before use; the sulfur is crushed to 60-160 mesh. Weigh 100 grams of screened active coke in proportion, and then weigh 5 grams of sulfur (according to the sulfur-to-carbon ratio of 5%), and manually mix and stir in a glass container.

[0045] Transfer the primary mixed active coke and sulfur samples into the special closed reactor for the test, fully tighten it and then shake it gently for secondary mixing, then place the closed reactor in the tubular resistance furnace, and connect the rotating system at both ends .

[0046] Set the test parameters related to the co-thermal modification load. In this example, the heating rate is set to 5°C / min, and the final reaction temperature is kept at 400°C for 4 hours. The reactor rotation frequency is 10Hz, and th...

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Abstract

The invention discloses a preparation method of a demercuration adsorbent based on activated coke and a product. The method comprises the following steps: mixing activated coke with a preset index and sulfur with a preset granularity according to a preset proportion to obtain a mixture; and placing the obtained mixture in a closed reactor, and carrying out a rotary co-heating reaction under preset process conditions to obtain a sulfur-loaded demercuration adsorbent. The basic carbon material adopted by the invention has specific porosity and granularity, can better adsorb and load the sulfur element, and improves the sulfur loading rate; the closed reactor is adopted in the technological process, so that waste of sulfur resources is prevented; and the rotary dynamic co-heating reaction is adopted, so that the sulfur element loading uniformity is good, and the product consistency is relatively high. The method is simple to operate, efficient and suitable for industrial production. Therefore, the technical problems of low sulfur loading rate, non-uniform loading and poorer product quality consistency of existing preparation methods of demercuration adsorbents are solved.

Description

technical field [0001] The invention relates to the technical field of preparation of mercury removal adsorbent, in particular to a preparation method and product of a mercury removal adsorbent based on active coke. Background technique [0002] Mercury is highly toxic, accumulative, persistent and long-distance migration, and has always been the focus and difficulty of environmental governance. According to the "2018 Global Mercury Assessment Report" of the United Nations Environment Programme, the current global annual mercury emissions are about 2,220 tons, and Asia accounts for about 40% of the total mercury emissions. China is the world's largest mercury production, use and emission country . In October 2013, China formally signed the Minamata Convention on Mercury, which came into effect globally in August 2017, which means that my country will gradually increase its requirements for flue gas control and environmental monitoring related to mercury pollution. At prese...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/28B01J20/20B01J20/30B01D53/02
CPCB01J20/28016B01J20/28061B01J20/28064B01J20/28004B01J20/20B01J20/30B01D53/02B01D2258/0283B01D2257/602B01D2253/102
Inventor 昌健龚得喜吕小玲严铭魏艳立左文华
Owner BEIJING SPC ENVIRONMENT PROTECTION TECH