CN108043466A - One kind is used for NOxThe zeolite imidazole ester skeleton structure composite material and preparation method and application of removing - Google Patents

One kind is used for NOxThe zeolite imidazole ester skeleton structure composite material and preparation method and application of removing Download PDF

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CN108043466A
CN108043466A CN201711428921.8A CN201711428921A CN108043466A CN 108043466 A CN108043466 A CN 108043466A CN 201711428921 A CN201711428921 A CN 201711428921A CN 108043466 A CN108043466 A CN 108043466A
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composite material
skeleton structure
structure composite
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imidazole ester
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CN108043466B (en
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王睿
陈永亮
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Shandong University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/1691Coordination polymers, e.g. metal-organic frameworks [MOF]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8621Removing nitrogen compounds
    • B01D53/8625Nitrogen oxides
    • B01D53/8628Processes characterised by a specific catalyst
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/90Injecting reactants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0234Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
    • B01J31/0235Nitrogen containing compounds
    • B01J31/0244Nitrogen containing compounds with nitrogen contained as ring member in aromatic compounds or moieties, e.g. pyridine
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
    • B01J37/10Heat treatment in the presence of water, e.g. steam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/20Reductants
    • B01D2251/206Ammonium compounds
    • B01D2251/2062Ammonia
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/02Compositional aspects of complexes used, e.g. polynuclearity
    • B01J2531/0238Complexes comprising multidentate ligands, i.e. more than 2 ionic or coordinative bonds from the central metal to the ligand, the latter having at least two donor atoms, e.g. N, O, S, P
    • B01J2531/0241Rigid ligands, e.g. extended sp2-carbon frameworks or geminal di- or trisubstitution
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/70Complexes comprising metals of Group VII (VIIB) as the central metal
    • B01J2531/72Manganese

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Inorganic Chemistry (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses one kind to be used for NOxThe zeolite imidazole ester skeleton structure composite material and preparation method and application, preparation method of removing include the following steps:After raw material needed for the soluble-salt of manganese, synthetic zeolite imidazate skeleton structure composite material and solvent mixing, the zeolite imidazole ester skeleton structure composite material of Mn oxide modification is prepared using solvent-thermal method;Solvent, the soluble-salt of manganese and the mass ratio of raw material needed for synthetic zeolite imidazate skeleton structure composite material are 8 10:0.2‑0.75:1.The composite material of the present invention avoids Mn oxide reunion inactivation under reaction temperature by means of the larger surface area of zeolite imidazole ester skeleton structure composite material, temperature window is widened, it realizes and removes the efficient catalytic of nitrogen oxides at a lower temperature, improve the catalytic activity of catalyst.

Description

One kind is used for NOxThe zeolite imidazole ester skeleton structure composite material and preparation method of removing And application
Technical field
It is more particularly to a kind of to be used for NO the invention belongs to atmosphere pollution control technology fieldxThe Mn oxide of removing is repaiied The zeolite imidazole ester skeleton structure composite material and preparation method and application of decorations.
Background technology
Nitrogen oxides (mainly includes NO and NO2) it is a kind of common gas pollutant, improvement is always for a long time The important content of environmental protection, source are broadly divided into moving source and stationary source, and stationary source refers mainly to the combustion of the fossils such as industrial production The flue gas that the burning of material is discharged (such as the burning of coal and oil), moving source refer mainly to the discharge of motor-vehicle tail-gas.With modern age Industrialized fast development, fossil fuel are largely developed and used so that be discharged into nitrogen oxides in air considerably beyond The bearer cap and self-purification capacity of atmospheric environment.Nitrogen oxides is very big to environmental hazard, for example, photochemical fog, acid rain and Ozone hole is related with the discharge of nitrogen oxides, threatens the life security of human and animal.Therefore, it is necessary to strengthen administering air In nitrogen oxides.
At present, industrial most commonly seen, the Treatment process for the NOx being most widely used is mainly with NH3For reducing agent Selective catalytic reduction (NH3-SCR).Catalyst is the key factor for influencing SCR denitration efficiency.Currently used catalyst Mainly include noble metal catalyst, molecular sieve catalyst, metal oxide catalyst.Wherein V2O5-WO3/TiO2It is common at present Commercial catalyst, the catalyst have higher catalytic activity in 350-500 DEG C of temperature window, but in practical applications, it should It is higher with cost, and active component vanadium is volatilized at high temperature with bio-toxicity, and environment and the mankind are caused to poison, moreover, right The temperature requirement of pending nitrogen oxides is higher, is difficult to obtain good catalyticing purifying effect under low temperature.Therefore exploitation low temperature is high It is extremely urgent to imitate non-toxic catalyst.
The content of the invention
Technical problem present in for the above-mentioned prior art, the object of the present invention is to provide one kind to be used for NOxRemoving Zeolite imidazole ester skeleton structure composite material and preparation method and application.
In order to solve the above technical problems, the technical scheme is that:
One kind is used for NOxThe preparation method of the zeolite imidazole ester skeleton structure composite material of removing, includes the following steps:
After raw material needed for the soluble-salt of manganese, synthetic zeolite imidazate skeleton structure composite material and solvent mixing, adopt The zeolite imidazole ester skeleton structure composite material of Mn oxide modification is prepared with solvent-thermal method;
Solvent, the soluble-salt of manganese and the mass ratio of raw material needed for synthetic zeolite imidazate skeleton structure composite material are 8- 10:0.2-0.75:1.
Preferably, the soluble-salt of the manganese is manganese nitrate.Research shows compared with manganese chloride, manganese acetate, uses nitre Catalyst activity higher prepared by sour manganese.
Preferably, the solvent is more than 99.5% absolute methanol for content.Classical zeolite imidazole ester skeleton structure material Solvent used in the synthesis of material be absolute methanol and n,N-Dimethylformamide, and it has been investigated that, use N, N- dimethyl The zeolite imidazole ester skeleton structure composite material thermal stability of Mn oxide modification prepared by formamide is poor, in NH3- SCR is anti- Ying Zhong, catalytic activity just starts drastically to decline when temperature reaches 300 DEG C.
Preferably, the temperature of the solvent-thermal method is 135-145 DEG C, reaction time 20-30h.
Preferably, before being prepared using solvent-thermal method, ultrasonic pretreatment is carried out to the solution after mixing.Ultrasound can be located Reason can make active material manganese salt it is scattered evenly.
It is further preferred that the time of ultrasound pretreatment is 5-10min, supersonic frequency 20-40kHz.
Preferably, the preparation method further includes the step of being activated to the composite material being prepared, specific as follows: Dried composite material is put into tube furnace, is passed through nitrogen thereto, 250 are warming up to according to the rate of 5-10 DEG C/min DEG C, 3-5h is kept, the zeolite imidazole ester skeleton structure composite material modified after cooling up to the Mn oxide of high activity.
It is further preferred that the nitrogen is High Purity Nitrogen, the flow of nitrogen is 45-55mL/min.
The zeolite imidazole ester skeleton structure composite material for the Mn oxide modification that above-mentioned preparation method is prepared.
The zeolite imidazole ester skeleton structure composite material of above-mentioned Mn oxide modification is in catalysis NH3- SCR reaction removals NOx In application.
The zeolite imidazole ester skeleton structure composite material of above-mentioned Mn oxide modification is as catalyst NH3- SCR reacts Method, specifically comprise the following steps:
1) the zeolite imidazole ester skeleton structure composite material preforms for modifying the Mn oxide after activation are sieved, and make composite wood The grain size of material is 60-80 mesh, obtains catalyst;
2) pending flue gas is flowed through into catalyst, and NH is passed through into flue gas3As reducing agent, at 230-400 DEG C into Row denitration reaction.
Using the composite material as catalyst, it can realize that the high efficiency of nitrogen oxides in effluent takes off at a lower temperature It removes, the removal efficiency of nitrogen oxides is up to more than 90%.
Preferably, the NH being passed through in step 2)3Concentration be 500ppm.
Beneficial effects of the present invention
1st, composite material of the invention is avoided by means of the larger surface area of zeolite imidazole ester skeleton structure composite material Mn oxide is reunited inactivation under reaction temperature, has been widened temperature window, has been realized nitrogen oxides at a lower temperature efficient Catalytic eliminating improves the catalytic activity of catalyst.
2nd, raw material of the present invention is easy to get, preparation method is simple, high catalytic efficiency, highly practical, easy to spread.
Specific embodiment
It is noted that following detailed description is all illustrative, it is intended to provide further instruction to the application.It is unless another It indicates, all technical and scientific terms used herein has usual with the application person of an ordinary skill in the technical field The identical meanings of understanding.
It should be noted that term used herein above is merely to describe specific embodiment, and be not intended to restricted root According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singulative It is also intended to include plural form, additionally, it should be understood that, when in the present specification using term "comprising" and/or " bag Include " when, indicate existing characteristics, step, operation, device, component and/or combination thereof.
Example 1:The preparation method of the zeolite imidazole ester skeleton structure composite material of Mn oxide modification
(1) precise 3.528g zinc nitrate hexahydrates, 1.944g methylimidazoles, 0.807g sodium formates, same to 78.5ml Absolute methanol mixes, magnetic agitation, and 50% manganese nitrate solutions of 1.5mL are added dropwise, and keeps magnetic agitation 5min.
(2) gained mixed solution handles 5min under 30kHz ultrasounds.
(3) in the reaction kettle for the polytetrafluoroethyllining lining that the mixed liquor of gained ultrasound pretreatment is put into 100mL, it is placed in baking oven In, it is to slowly warm up to 140 DEG C and keeps for 24 hours.
(4) gained suspension is after absolute methanol washs 3 times, the dry 8h in 60 DEG C of baking ovens.
(5) obtained solid powder is provided into tube furnace, after good seal, is passed through the High Purity Nitrogen of 50mL/min;Tube furnace is pressed 250 DEG C are warming up to according to the rate of 5 DEG C/min, 3h is kept, is taken out after natural cooling, you can obtains the Mn oxide modification of high activity Zeolite imidazole ester skeleton structure composite material.
Example 2:The preparation method of the zeolite imidazole ester skeleton structure composite material of Mn oxide modification
(1) precise 3.528g zinc nitrate hexahydrates, 1.944g methylimidazoles, 0.807g sodium formates, with 74ml without Water methanol mixes, magnetic agitation, and 50% manganese nitrate solutions of 6mL are added dropwise, and keeps magnetic agitation 5min.
(2) the lower processing 10min of gained mixed solution 30kHz ultrasounds.
(3) in the reaction kettle for the polytetrafluoroethyllining lining that the mixed liquor of gained ultrasound pretreatment is put into 100mL, it is placed in baking oven In, it is to slowly warm up to 140 DEG C and keeps for 24 hours.
(4) gained suspension is after absolute methanol washs 3 times, in 60 DEG C of dry 12h.
(5) obtained solid powder is provided into tube furnace, after good seal, is passed through the High Purity Nitrogen of 50mL/min;Tube furnace is pressed 250 DEG C are warming up to according to the rate of 5 DEG C/min, 5h is kept, is taken out after natural cooling, you can obtains the Mn oxide modification of high activity Zeolite imidazole ester skeleton structure composite material.
Comparative example 1
Difference with example 2 is:Omit the ultrasonic pre-treatment step of step (2).
Comparative example 2
Difference with example 2 is:Solvent in step (1) is N,N-dimethylformamide.
Comparative example 3
Difference with example 2 is:Omit the activation step of step (5).
Effect experiment
By example 1 and 2, the zeolite imidazole ester skeleton structure composite material of Mn oxide modification prepared by comparative example 1-3 is made It is used to be catalyzed NH for catalyst3- SCR reacts, and is as follows:
The zeolite imidazole ester skeleton structure composite material preforms that above-mentioned Mn oxide is modified are sieved, and take 0.3g grain sizes 60- 80 mesh catalyst, are put into quartz ampoule, are placed in tube furnace, and volume flow is 100mL/min by temperature programming instrument control system by temperature NO, O2And N2Mixed gas continue through quartz ampoule, wherein NO in gaseous mixture as the mixed gas of simulated flue gasxIt is dense It spends for 500ppm, while is passed through concentration as 500ppm NH3As reducing agent, carried out at 230 DEG C, 300 DEG C, 350 DEG C, 400 DEG C Denitration reaction, and pass through the oxides of nitrogen gas concentration in flue gas analyzer dynamic monitoring tail gas.The removing of specific nitrogen oxides Rate is as shown in table 1:
Table 1
230℃ 300℃ 350℃ 400℃
Example 1 91% 95% 93% 91%
Example 2 92% 95% 93% 90%
Comparative example 1 82% 84% 83% 80%
Comparative example 2 80% 65% 20% 14%
Comparative example 3 71% 78% 77% 67%
The experimental results showed that the zeolite imidazole ester skeleton structure composite material of Mn oxide modification prepared by the present invention exists To NO at 230-400 DEG CxRemoval efficiency up to more than 90%, and ultrasonic pre-treatment step, reaction dissolvent in preparation method and Activation step can all influence the catalytic performance of composite material.
The foregoing is merely the preferred embodiments of the application, are not limited to the application, for the skill of this field For art personnel, the application can have various modifications and variations.It is all within spirit herein and principle, made any repair Change, equivalent substitution, improvement etc., should be included within the protection domain of the application.

Claims (10)

1. one kind is used for NOxThe preparation method of the zeolite imidazole ester skeleton structure composite material of removing, it is characterised in that:Including such as Lower step:
After raw material needed for the soluble-salt of manganese, synthetic zeolite imidazate skeleton structure composite material and solvent mixing, use is molten The zeolite imidazole ester skeleton structure composite material of Mn oxide modification is prepared in the hot method of agent;
Solvent, the soluble-salt of manganese and the mass ratio of raw material needed for synthetic zeolite imidazate skeleton structure composite material are 8-10: 0.2-0.75:1。
2. preparation method according to claim 1, it is characterised in that:The soluble-salt of the manganese is manganese nitrate.
3. preparation method according to claim 1, it is characterised in that:The solvent is for content more than 99.5% without water beetle Alcohol.
4. preparation method according to claim 1, it is characterised in that:The temperature of the solvent-thermal method is 135-145 DEG C, instead It is 20-30h between seasonable.
5. preparation method according to claim 1, it is characterised in that:Before being prepared using solvent-thermal method, to mixing Solution afterwards carries out ultrasonic pretreatment;
Preferably, the time of ultrasound pretreatment is 5-10min, supersonic frequency 20-40kHz.
6. preparation method according to claim 1, it is characterised in that:It further includes and lives to the composite material being prepared It is the step of change, specific as follows:Dried composite material is put into tube furnace, is passed through nitrogen thereto, according to 5-10 DEG C/ The rate of min is warming up to 250 DEG C, keeps 3-5h, the zeolite imidazole ester skeleton modified after cooling up to the Mn oxide of high activity Structural composite material;
Preferably, the nitrogen is High Purity Nitrogen, and the flow of nitrogen is 45-55mL/min.
7. the zeolite imidazole ester skeleton structure for the Mn oxide modification that any preparation methods of claim 1-6 are prepared is answered Condensation material.
8. the zeolite imidazole ester skeleton structure composite material that Mn oxide described in claim 7 is modified is in catalysis NH3- SCR reactions are gone Except the application in NOx.
9. the zeolite imidazole ester skeleton structure composite material that Mn oxide described in claim 7 is modified is as catalyst NH3- The method of SCR reactions, it is characterised in that:Specifically comprise the following steps:
1) the zeolite imidazole ester skeleton structure composite material preforms for modifying the Mn oxide after activation are sieved, and make composite material Grain size is 60-80 mesh, obtains catalyst;
2) pending flue gas is flowed through into catalyst, and NH is passed through into flue gas3As reducing agent, denitration is carried out at 230-400 DEG C Reaction.
10. according to the method described in claim 9, it is characterized in that:The NH being passed through in step 2)3Concentration be 500ppm.
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