Desorption and regeneration method for organic matter adsorbent

A technology of adsorbent and organic matter, which is applied in the field of regeneration of organic pollutant adsorbent, can solve the problems of slow heat transfer rate, difficult storage and separation, and low dielectric constant, so as to reduce high-temperature hot spots and sparks, omit unit operation, Effect of reducing separation load

Inactive Publication Date: 2013-12-18
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, in industrial practice, water vapor regeneration technology also has several problems: (1) using the water vapor temperature to heat the adsorbent consumes a large amount of water vapor; Adsorbents such as resin and resin have small thermal conductivity, slow heat transfer rate, and long desorption time; (3) water molecules will remain in the adsorbent, and the adsorbent needs hot air to dry, which consumes a lot of energy; (4) desorption The product has a high water content, which makes subsequent storage and separation difficult
However, microwave treatment also has some limitations: (1) First, microwave treatment of media with high dielectric constant such as activated carbon is prone to local high temperature and sparks, which has serious safety hazards and will destroy the structure of the adsorbent; (2) Compared with Highly hydrophobic adsorbents (such as resins, highly hydrophobic zeolite molecular sieves) and non-polar adsorbates (benzene, toluene), due to the low dielectric constant, microwaves can hardly heat these media, so good desorption can not be achieved. with effect

Method used

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  • Desorption and regeneration method for organic matter adsorbent
  • Desorption and regeneration method for organic matter adsorbent

Examples

Experimental program
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Effect test

Embodiment 1

[0025] Get 2 grams of activated carbon fibers, absorb 2 grams of toluene, and pack into a desorption tower, such as figure 1 to build a desorption device. The desorption tower 6 is provided with a microwave generator 5, and the steam generator 1 is communicated with the steam inlet at the top of the desorption tower 6 through a flow meter, and the nitrogen generator 7 is communicated with the nitrogen inlet at the top of the desorption tower 6 through a flow meter, and the nitrogen gas The outlet and the steam outlet are respectively arranged at the bottom of the desorption tower 6, the steam outlet is connected to the condenser 2, and the outlet of the condenser 2 is connected to a storage container 3 for storing liquid organic matter and water condensed from the condenser. The pipeline between the steam generator 1 and the steam inlet at the top of the desorption tower 6 is provided with an insulation jacket 4 to prevent steam from condensing.

[0026] Desorption is perform...

Embodiment 2

[0032]Take 2 grams of Y-type molecular sieves, absorb 2 grams of toluene, put them into a microwave desorption tower, and perform desorption according to the three methods of Example 1: (1) Microwave + water vapor, microwave power is 600W, water vapor flow rate is 1.0g / min; (3) microwave + nitrogen, nitrogen air velocity 2000h -1 ; (2) Water vapor, water vapor flow rate 1.0g / min.

[0033] The desorption rate comparison results of the above three methods are shown in image 3 , the results show that under the action of microwave, toluene on the surface of Y molecular sieve can be completely desorbed within 10 minutes. Under the synergistic effect of water vapor and microwave, the desorption rate is faster than single microwave, and the desorption can be completed within 7 minutes. However, it takes nearly 30 minutes to desorb completely by using a single water vapor desorption. Therefore, for Y molecular sieve adsorbents with a certain polarity, microwave can significantly ...

Embodiment 3

[0035] Take 2 grams of porous polymer resin polydivinylbenzene (PDVB), absorb 10 grams of toluene, put it into a microwave desorption tower, and perform desorption according to the three methods of Example 1: (1) microwave + water vapor, microwave power is 600W, water vapor flow rate 1.0g / min; (3) microwave + nitrogen, nitrogen air velocity 2000h -1 ; (2) Water vapor, water vapor flow rate 1.0g / min.

[0036] The desorption rate comparison results of the above three methods are shown in Figure 4 , found that under the action of a single microwave, the desorption rate of toluene on the resin surface was very slow, and after 30 minutes, the desorption rate only reached 40%. However, under the synergistic effect of water vapor and microwave, the desorption rate is greatly improved compared with single microwave, and the desorption can be completed within 5 minutes. However, it takes nearly 30 minutes to desorb completely by using a single water vapor desorption. Therefore, for...

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Abstract

The invention discloses a desorption and regeneration method for an organic matter adsorbent. The method is characterized in that an organic matter adsorbent desorption and regeneration device of a microwave generator is arranged in a desorption tower; the to-be-desorbed adsorbent with organic matters is put in the desorption tower; steam is aerated from the top of the desorption tower; the microwave generator is started, wherein the microwave power is 500-10000W; desorption is carried out for 2-30 minutes; the desorbed organic matters and steam flow out from a steam outlet at the bottom of the desorption tower and enter a condenser for condensation; then the steam is cut off, nitrogen is aerated from the top of the desorption tower, and the nitrogen flows out from the bottom, wherein the microwave power is 200-2000W; drying treatment is carried out for 2-20 minutes; the microwave generator is turned off, and the nitrogen is cut off; the desorbed adsorbent is obtained. According to the method, the desorption rate is improved by a large margin by combining steam and the microwave technology, and less desorption residue is left.

Description

(1) Technical field [0001] The invention relates to a regeneration method of an organic pollutant adsorbent, especially aimed at the regeneration and desorption of organic molecules in activated carbon, molecular sieves and polymer resin adsorbents, and solves the current problem of adsorbent regeneration after adsorption of organic waste gas and organic waste water. (2) Background technology [0002] Adsorption technology is currently widely used in the treatment of organic waste gas and organic wastewater, especially for some low-concentration organic waste gas and wastewater. Adsorption can remove organic pollutants well and achieve the purpose of purification. In addition, through desorption and recycling, the resource utilization of organic pollutants can also be realized. At present, the most common adsorbents in the industry include activated carbon, activated carbon fiber, zeolite molecular sieve and polymer porous resin, etc., and these adsorbents all show good adso...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/34B01J19/12
Inventor 卢晗锋常仁琴周瑛曹洁晶刘露杰黄海凤陈银飞楚建堂季雪阳方敏杰
Owner ZHEJIANG UNIV OF TECH
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