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CN-224207768-U - Adsorption cylinder and adsorption bed structure for catalytic adsorption and purification of gas

CN224207768UCN 224207768 UCN224207768 UCN 224207768UCN-224207768-U

Abstract

The utility model discloses an adsorption cylinder for catalytic adsorption and purification of gas, which is cylindrical and is characterized in that a plurality of purification flow channels with sections gradually becoming smaller inwards are uniformly distributed on the peripheral wall of the adsorption cylinder, and a layer of catalytic adsorption material is arranged on the inner wall of the purification flow channel. Also discloses an adsorption bed structure adopting the adsorption cylinder. The adsorption cylinder and the adsorption bed structure thereof disclosed by the utility model realize adsorption based on the arc-shaped reduced purification flow channel, can better improve the adsorption treatment purification efficiency, can enable the adsorption rate of each position to be matched with the consumption rate of the adsorption material so as to improve the utilization efficiency of the adsorption material and facilitate the regeneration treatment of the adsorption material.

Inventors

  • WU DAN
  • HU PENGBO
  • ZHANG YINGZI
  • FENG CHI
  • WENG QIYU

Assignees

  • 西南交通大学
  • 重庆大学

Dates

Publication Date
20260508
Application Date
20250603

Claims (10)

  1. 1. The utility model provides an adsorption cylinder for gas catalytic adsorption purifies, adsorption cylinder is cylindric, its characterized in that, evenly distributed is provided with a plurality of cross-section purification runner that inwards diminishes gradually on the adsorption cylinder periphery wall, purification runner inner wall is provided with one deck catalytic adsorption material.
  2. 2. The cartridge for catalytic adsorption purification of a gas according to claim 1, wherein the innermost end of the purification flow channel is in communication with the interior of the cartridge through a porous structure carrying catalytic adsorbent material.
  3. 3. The cartridge for catalytic adsorption purification of a gas according to claim 1, wherein the purification flow path is spirally and inwardly extended along a circumferential direction of the cartridge.
  4. 4. The adsorption cartridge for catalytic adsorption purification of a gas according to claim 1, wherein the purification flow path is provided obliquely from top to bottom as a whole.
  5. 5. The adsorption cartridge for catalytic adsorption purification of a gas according to claim 1, wherein the adsorption cartridge is made of a porous material and is internally loaded with a part of the adsorption purification material.
  6. 6. The adsorption cylinder for catalytic adsorption purification of gas according to claim 1, wherein the inside and the outside of the adsorption cylinder are each provided with a catalytic adsorption material layer, and a weak area through which the gas can pass is provided at a position of the catalytic adsorption material layer inside the adsorption cylinder corresponding to the inner end of the purification flow passage.
  7. 7. The adsorption cartridge for catalytic gas adsorption purification according to claim 1, wherein the purification channels are uniformly distributed in rows in the circumferential direction, and the purification channels have a vertically rectangular cross section.
  8. 8. The adsorption cylinder for catalytic adsorption purification of gas according to claim 7, wherein the adsorption cylinder is axially layered, the layered surface is conical ring-shaped, and the purification flow channel is arranged on the layered surface of the upper layer and the lower layer.
  9. 9. An adsorption bed structure comprising a baffle plate arranged along the cross section of an airflow channel, wherein a plurality of air passing holes are uniformly distributed on the baffle plate, and the adsorption bed structure is characterized in that an adsorption cylinder as claimed in any one of claims 1-8 is vertically and fixedly arranged outside the peripheral position of each air passing hole on one side of the baffle plate in the air inlet direction, and one end, far away from the baffle plate, of the adsorption cylinder is hermetically arranged.
  10. 10. The adsorbent bed structure of claim 9, wherein the gas flow channels are vertically arranged, the lower ends of the gas flow channels are gas outlet ends, cover plates are arranged at the upper ends of the adsorption cylinders far away from the partition plates to realize sealing, a pressing net is integrally arranged at the upper ends of the cover plates, and the periphery of the pressing net is detachably fixed on the inner wall of the gas flow channels.

Description

Adsorption cylinder and adsorption bed structure for catalytic adsorption and purification of gas Technical Field The utility model relates to the technical field of gas purification equipment, in particular to an adsorption cylinder and an adsorption bed structure for gas catalytic adsorption purification. Background Catalytic filtration purification is a conventional method of gas purification treatment. In the existing gas catalytic filtration and purification treatment technology, layered catalytic purification adsorbent particle materials are generally arranged in a gas flow channel to form an adsorbent bed, and then gas to be treated is driven to flow through the adsorbent bed, so that harmful components in the gas to be purified and the adsorbent are contacted and reacted, and the harmful components are trapped to realize filtration and purification. In some technologies, the adsorbent particles are supported on the porous material to form an adsorption material, but during the adsorption treatment, the gas to be treated is still driven to pass through the adsorption material for adsorption treatment. In the existing catalytic adsorption filtration mode, the gas to be treated generally passes through the adsorbent material in a unidirectional vertical direction, and the problems generally exist that 1 the contact-collision-reaction filtration flow of the gas to be treated and the adsorbent material is short, and the adsorption filtration efficiency is difficult to improve. 2 the gas to be treated passes through the adsorbent material in the vertical direction, so the reaction efficiency of the contact part of the adsorbent material and the gas to be treated is higher, the reaction efficiency of the contact part of the adsorbent material and the gas to be treated is lower, the non-uniformity of the reaction efficiency before and after the reaction efficiency can lead to the difficulty in controlling the whole regeneration time of the adsorbent, the non-uniformity of the purification efficiency before and after the reaction efficiency, and the whole purification effect and efficiency are reduced. And 3, the gas to be treated uniformly passes through the adsorbent material, and after the contact reaction between the adsorbent material at the front side and harmful substances, the volume is increased and pore channels are blocked, so that the blocking is caused, and the purification reaction efficiency of the subsequent adsorbent material is reduced. Therefore, how to better improve the adsorption efficiency, improve the utilization efficiency of the adsorbent material and facilitate the regeneration treatment of the adsorbent material is a direction of long-term effort improvement of the technicians in the field of catalytic adsorption, purification and filtration. Disclosure of utility model Aiming at the defects of the prior art, the utility model aims to provide an adsorption cylinder and an adsorption bed structure for gas catalytic adsorption purification, which can better improve the adsorption treatment purification efficiency, improve the utilization efficiency of an adsorbent material and facilitate the regeneration treatment of the adsorbent material. In order to solve the technical problems, the utility model adopts the following technical scheme: An adsorption cylinder for catalytic adsorption and purification of gas, which is cylindrical, is characterized in that, the adsorption cylinder is characterized in that a plurality of purification flow channels with sections gradually becoming smaller inwards are uniformly distributed on the peripheral wall of the adsorption cylinder, and a layer of catalytic adsorption material is arranged on the inner wall of each purification flow channel. In this way, the catalytic adsorption purification material is arranged on the inner wall of the purification flow channel with the diameter gradually decreasing in the advancing direction, so that the catalytic adsorption purification material contacts with the passing gas to realize the reaction purification of harmful components. When the gas is positioned at the inlet position of the rear end of the purifying flow channel, the corresponding purifying material area on the inner wall of the purifying flow channel is larger, and the cross section of the purifying flow channel is gradually reduced along with the forward flow of the gas along with the purifying flow channel, the area for adsorbing the purifying material is reduced, but the content of harmful components is also reduced along with the gradual purification of the gas, and the flow velocity is increased after the cross section of the purifying flow channel is reduced. Therefore, the purification rates at the front and rear parts of the purification flow channel can be kept high in consistency, the use uniformity of the adsorption material is improved, and the purification efficiency of the adsorption treatment can be better improved. Further, the i