Method for improving adsorption capability of fixed bed and application method thereof in organic waste gas treatment

Patent metadata

Field	Value
Publication number	US-10486098-B2
Application number	US-201615742380-A
Country	US
Kind code	B2
Filing date	Aug 11, 2016
Priority date	Aug 19, 2015
Publication date	Nov 26, 2019
Grant date	Nov 26, 2019

Abstract

The present invention disclosed a method for improving the adsorption capacity of a fixed bed and its application in organic waste gas treatment field. The steps are: (1) adsorption: organic waste gas is passed through the adsorption column containing the adsorbent to allow the organic waste to be adsorbed; when VOCs concentration at the outlet end of the adsorption column reached a preset value, the adsorption is halted; (2) desorption: adsorbent that has absorbed VOCs was desorbed by water vapor of 110° C. or higher, or hot nitrogen of 150° C. or higher; the desorbed VOCs enter into a condenser and is recovered in liquid state; (3) pre-adsorption of water: spray water inside the adsorption column after the desorption to adjust the water content of the adsorbent to 8-35%, no other treatment is necessary before the next batch of VOCs adsorption.

First claim

What is claimed is:

1. A method for improving the adsorption capacity of a fixed bed as applied in the field of organic gas waste adsorption treatment, comprising the steps of:
(1) adjusting an initial water content of an adsorbent so that the initial water content is in the range of 8-35 WT %;
(2) adsorbing, wherein an organic waste gas is passed into an adsorption column loaded with the adsorbent and absorbed by the adsorbent;
(3) desorbing, wherein the adsorbent that has adsorbed the organic waste from step 2 is desorbed, and the desorbed organic waste is let into a condenser and collected in liquid form;
(4) pre-adsorbing water, wherein water is sprayed inside the adsorption column and water content of the absorbent in the desorbed adsorption column is adjusted; and
(5) re-adsorbing, wherein the adsorbent that has pre-adsorbed water in step 4 is applied to adsorb an organic waste gas as in step 2.

2. A method for improving the adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein a temperature increase in the fixed bed is reduced; and wherein the adsorbent is a macroporous adsorption resin with a backbone made from styrene-divinylbenzene copolymer or an ultra-high cross-linked adsorption resin.

3. A method for improving the adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein the temperature increase in the fixed bed is reduced; and wherein the adsorbent is a molecular sieve with a silica to alumina ratio equal or higher than 30 or a fully-silicated molecular sieve.

4. A method for improving the adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein the temperature increase in the fixed bed is reduced; and wherein the absorbing is operated under normal temperature and normal pressure, and the adsorption is halted when the concentration of the organic waste gas at an outlet of the adsorption column reaches a preset value.

5. A method for improving adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein the temperature increase in the fixed bed is reduced; and further comprising the steps of:
spraying water inside the adsorption column loaded with the adsorbent and adjusting the water content of the adsorbent; and
passing the organic waste gas into the adsorption column loaded with the adsorbent to adsorb the organic wastes.

6. A method for improving the adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein the temperature increase in the fixed bed is reduced; and wherein the desorbing is performed by water vapor of 110° C. or higher, or by hot nitrogen of 150° C. or higher.

7. A method for improving the adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein the temperature increase in the fixed bed is reduced; and wherein the water content of the absorbent in the desorbed adsorption column is adjusted to 8-35 WT %.

8. A method for improving the adsorption capacity of the fixed bed according to claim 1 , as applied in the field of organic gas waste adsorption treatment, wherein the temperature increase in the fixed bed is reduced; and further comprising operating two or more adsorption columns loaded with the adsorbent, wherein one of the two or more adsorption columns undergoes the step 2 of claim 1 , whereas the rest of the two or more adsorption column undergoes the steps 3 or 4 of claim 1 , in substantially contemporaneous manner.

Assignees

• Nanjing University Of Technology

Inventors

• Long Chao
• He Honglei
• Yao Xiaohong
• Wu Jian
• Jia Lijuan
• Wu Liuyan

Classifications

• B01D53/0454

  Controlling adsorption (controlling temperature swing adsorption B01D53/0462, controlling pressure swing adsorption B01D53/047) · CPC title

• B01D53/0423 Primary

  Beds in columns · CPC title

• B01D2257/80

  Water · CPC title

• B01D2257/708

  Volatile organic compounds V.O.C.'s · CPC title

• B01D2259/402

  using two beds · CPC title