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Regenerated flue gas dechlorinating agent and preparation method thereof

A technology for regenerating flue gas and dechlorination agent, applied in separation methods, chemical instruments and methods, and other chemical processes, can solve problems such as poor high temperature stability and low dechlorination efficiency, achieve strong stability, convenient application, and improve Effect of Pore Volume and Specific Surface Area

Pending Publication Date: 2022-07-22
QINGDAO UNIV OF SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to solve the problems of poor high temperature stability and low dechlorination efficiency in the above-mentioned prior art dechlorination method, and propose a regenerated flue gas dechlorination agent and a preparation method thereof, using a modified molecular sieve as a carrier, through Post-treatment changes its surface acidity. Through ion modification and introduction of inert release agent, the chlorine capacity and high-temperature service stability of the molecular sieve dechlorination agent are effectively improved, and the cost is further reduced while meeting the dechlorination requirements of the regenerated flue gas.

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0031] This embodiment provides a regenerative flue gas dechlorinating agent, in terms of mass percentage, the components include: 20% modified 13X molecular sieve carrier, 60% calcium carbonate and sodium carbonate (the mass ratio of the two is 3:1) , 10% citric acid and activated clay (the mass ratio of the two is 1:1), 0.5% calcium aluminate and 9.5% PEG-1000 and sodium carboxymethyl cellulose (the mass ratio of the two is 1:1) .

[0032] The modification reaction steps of the modified 13X molecular sieve are as follows: mix 13X molecular sieve and 1 mol / L ammonium chloride solution in a ratio of 1 g: 30 ml, exchange at 100 ° C for 20 min, repeat the exchange for 2 times, roast at 550 ° C for 6 hours, and then use metal A cerium nitrate solution with a loading of 3% was ion-exchanged at 80°C for 8h and calcined at 450°C for 4h to prepare a carrier.

[0033] The present embodiment also provides a preparation method of a regenerative dechlorination agent, comprising the foll...

Embodiment 2

[0039]This embodiment provides a regenerative flue gas dechlorinating agent, which, in terms of mass percentage, comprises: 25% modified Y molecular sieve carrier, 55% calcium carbonate, sodium carbonate and magnesium oxide (calcium carbonate, sodium carbonate and The mass ratio of magnesium oxide is 3:1:1), 15% of citric acid and activated clay (the mass ratio of the two is 2:1), 1.0% of calcium silicate and 4.0% of PEG-1000 and PEG-800 ( The mass ratio of the two is 1:1).

[0040] The modification reaction steps of the modified Y molecular sieve are as follows: take Y molecular sieve and 1 mol / L ammonium chloride solution and mix at a ratio of 1 g: 20 ml, exchange at 100 ° C for 18 min, repeat the exchange for 2 times, calcinate at 450 ° C for 5 hours, and then use metal The lanthanum nitrate solution with the loading amount of 1% was ion-exchanged at 75°C for 7h, and calcined at 430°C for 3h to prepare the carrier.

[0041] The present embodiment also provides a preparatio...

Embodiment 3

[0048] This embodiment provides a regenerative flue gas dechlorination agent. In terms of mass percentage, the components include: 30% of modified 13X molecular sieve and modified Y molecular sieve carrier (the mass ratio of the two is 1:1), 50% of Calcium carbonate, sodium carbonate and magnesium oxide (the mass ratio of the three is 9:3:1), 17.5% citric acid and activated clay (the mass ratio of the two is 1:2), 1.5% calcium aluminate and 1.0% PEG-1000 and PEG-800 (the mass ratio of the two is 1:1).

[0049] The modification reaction steps of modified 13X and Y molecular sieves are as follows: take 13X molecular sieve and Y molecular sieve with a mass ratio of 1:1 and mix, then mix with 1mol / L ammonium chloride solution in a ratio of 1g:40ml, and exchange at 100 ° C for 22min , repeated the exchange for 2 times, calcined at 550 °C for 7 h, and then used silver nitrate solution with a metal loading of 5% to ion exchange at 85 °C for 10 h and calcined at 470 °C for 5 h to prep...

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Abstract

The invention belongs to the technical field of dechlorinating agents, and relates to a regenerated flue gas dechlorinating agent and a preparation method thereof, the dechlorinating agent comprises the following components by mass: 20%-30% of a carrier, 50%-60% of an active component, 10%-25% of an auxiliary agent, 0.5%-1.5% of an inert separant, and 1%-10% of a pore forming agent; the sum of the mass percentages of the components is 100%. According to the prepared regenerated flue gas dechlorinating agent, the modified molecular sieve is adopted as a carrier, the rich pore channel structure of the molecular sieve is optimized, the pore volume and the specific surface area are increased, the surface acidity of the molecular sieve is enhanced, and the combination degree of the modified molecular sieve carrier and active components is enhanced; when multiple active components are loaded on the molecular sieve to prepare the dechlorinating agent for use, the adsorption activity of the dechlorinating agent is improved, and meanwhile, due to the addition of the inert separant and the auxiliaries, the sintering of the active components is prevented, so that the whole structure of the dechlorinating agent is more stable, the maximization of the chlorine capacity of the dechlorinating agent is effectively realized, and the dechlorinating agent has the characteristic of high temperature and high water resistance.

Description

technical field [0001] The invention belongs to the technical field of dechlorination agents, and in particular relates to a regenerated flue gas dechlorination agent and a preparation method thereof. Background technique [0002] During the catalytic reforming reaction, with the prolongation of the reaction time, the activity of the catalyst decreases, and the chlorine on the catalyst also gradually loses. In order to maintain a certain acidity of the catalyst, keep the chlorine content on the catalyst stable, and maintain the high activity of the catalyst, it is necessary to continuously inject organic chlorine during the catalyst regeneration process. The catalyst will produce water during the coking process, and the water will take away the chloride ions on the catalyst, so the chlorine in the regeneration flue gas will cause the corrosion of the downstream process pipeline, and at the same time, the discharge into the air will also cause environmental pollution, which i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/18B01J20/28B01J20/30B01D53/04
CPCB01J20/18B01J20/043B01J20/041B01J20/12B01J20/04B01J20/186B01J20/28019B01D53/04B01D2257/2045
Inventor 王广建王芳谷杰韩德志邴连成
Owner QINGDAO UNIV OF SCI & TECH
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