CN1248490A - Catalyst for eliminating nitrogen oxide by means of microwave catalysis - Google Patents
Catalyst for eliminating nitrogen oxide by means of microwave catalysis Download PDFInfo
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- CN1248490A CN1248490A CN 98114335 CN98114335A CN1248490A CN 1248490 A CN1248490 A CN 1248490A CN 98114335 CN98114335 CN 98114335 CN 98114335 A CN98114335 A CN 98114335A CN 1248490 A CN1248490 A CN 1248490A
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- catalyst
- molecular sieve
- microwave
- indium
- iron oxide
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Abstract
The present invention relates to a catalyst used for microwave catalysis to eliminate nitrogen oxide compound, and is characterized by that the first active component of said catalyst is indium which is supported on the natural or artificial synthetic molecular sieve, and the silicon-aluminium ratio of the molecular sieve is less than 50, and the weight percentage content of indium supported by molecular sieve is 0.5-20%, and the wave-absorbing material which is higher in dielectric constant and can resist high-temp. oxidation is added as microwave carrier. This carrier can select iron oxide, the iron is second active component of said catalyst, and the weight ratio of molecular sieve and iron oxide is 10 : 0.5--10 : 20. Said invention is applicable to microwave catalysis to eliminate nitrogen oxide compound in the presence of large quantity of oxygen gas.
Description
The present invention relates to the environmental protection problem, employed microwave catalyst, preparation method and microwave catalysis process when a kind of elimination oxynitrides (NOx) is provided especially.
Environmental Pollution and Control is the problem of attracting worldwide attention, therefore, and as one of main aspect of atmosphere pollution, oxynitrides (NOx, i.e. NO and NO
2) elimination received the concern of countries in the world.It is the purification techniques of at present most widely used in the world processing oxynitrides that catalysis is eliminated.Hydro carbons selective reduction NOx (SCR) is acknowledged as the method that NOx has the application future most of eliminating now.And natural gas (its main component is a methane) reserves are abundant, more than the easier acquisition of other hydro carbons, not only be widely used in industrial production, and almost be present in the tail gas of each fuel, therefore, be a kind of practicality and inexpensive method with methyl hydride catalyzed reducing NOx.The patent of USP5149112 points out that under the oxygen-containing atmosphere, an amount of methane is reducing agent, and the Co-ZSM-5 activity of ion-exchange preparation is best.JP06,262,039 propose under the indium catalyst action that ZSM5 molecular sieve or ferrierite support, when aerobic exists, reducing agent methane and carbon monoxide act on simultaneously, oxynitrides can effectively be removed, JP06,132, what 139 proposition ZSM5 were molecular sieve supported is the indium catalyst of auxiliary agent with alkali metal, when aerobic existed, methane was made reducing agent, and loaded In/HZSM5 has higher conversion ratio to oxynitrides.In addition, relevant document has also reported with methane to be reducing agent, and under the oxygen existence condition, the NOx conversion ratio of catalyst such as Ga/HZSM5, Pd/HZSM5 is also higher.But along with the increase of oxygen concentration, gas space velocity, such activity of such catalysts all descends greatly.At the problems referred to above, the new way of oxynitrides all explore to be eliminated in countries in the world, and it has been one of method emerging since the nineties that microwave catalysis is eliminated NOx.U.S. FORD company and Canadian Queens University have at first been carried out the laboratory principle research of microwave catalysis processing vehicle exhaust in the world in 93 years, the catalyst that is adopted is Pt/Cordierite or Pd/Cordierite, because this catalyst is to the utilization rate too low (＜30%) of microwave, do not achieve satisfactory results, only improve 5% than conventional treatment method; USP5246554, USP5256265, the USP5269892 patent is pointed out, utilizes active carbon as catalyst, and simultaneously again as reducing agent, microwave catalysis is eliminated NOx, and conversion ratio can reach 90%; China's application number is the microwave purifying catalyst for automobile tail gas of microwave carrier for the NO.961194863 patent proposes with SiC, and under 800 watts of microwave actions, the NOx conversion ratio can reach more than 80%.
The object of the present invention is to provide a kind ofly under a large amount of oxygen existence conditions, be applicable to the novel microwave catalyst of the efficient elimination oxynitrides of microwave catalysis.
The invention provides a kind of under a large amount of oxygen existence conditions, be applicable to that microwave catalysis efficiently eliminates the novel microwave catalyst of oxynitrides, it is characterized in that: first active component of this catalyst is an indium, be supported on the natural or artificial synthetic molecular sieve, the silica alumina ratio of molecular sieve is less than 50, and the weight percentage of molecular sieve supported indium is 0.5～20%; It is higher to add dielectric constant, and the absorbing material of high temperature oxidation resisting is as microwave carrier, and this kind carrier is chosen as iron oxide, and iron is second active component of this catalyst, and the weight ratio of molecular sieve and iron oxide is 10: 0.5～10: 20.
Catalyst provided by the invention can be by the indium salt (In (NO with solubility
3)
3Or InCl
3) adopt infusion process to make with the mixture of molecular sieve and iron oxide, also can be with In
2O
3Adopt mechanical mixing to make 550～900 ℃ of sintering temperatures, 3～6 hours time with the mixture of molecular sieve and iron oxide.Catalyst provided by the invention is used in the eliminating nitrogen oxide by means of microwave catalysis reaction, is reducing agent with methane, [CH
4]/[NO] concentration ratio is 0.2～8.0, the unstripped gas air speed is 1000～100000h
-1, reaction pressure is a normal pressure.Oxygen concentration the best is between 2.0～10.0%.Microwave catalyst provided by the invention is the activity of such catalysts component with indium, iron only, is the microwave carrier of catalyst with the iron oxide only, and reactivity worth is good when low temperature, and the oxynitrides conversion ratio can reach 100%.Moreover, the present invention also provides a kind of new microwave catalysis mechanism, a kind of microwave carrier that can use in the microwave catalysis reaction promptly is provided, it has quick accumulation, transforms and passes to the ability of reaction molecular to microwave energy, and between catalytic surface and remaining reaction system, produce thermograde, make the product molecule hightail high temperature reaction zone, give full play to the microwave catalysis effect.Method for preparing catalyst provided by the invention is simple, and the existing ripe production specifications of required microwave catalysis device help technology and amplify, and eliminating commercial Application for the microwave catalysis of oxynitrides has great Practical significance.Below by embodiment in detail the present invention is described in detail.
Embodiment 1 Preparation of catalysts
Here only to contain indium 5% (weight percentage), the weight ratio of molecular sieve and iron oxide is 10: 4 In/HZSM5+Fe
2O
3(silica alumina ratio is 25) describes the preparation of microwave catalyst used among the present invention prevailingly for example.The HZSM5 molecular sieve is provided by Catalyst Factory, Nankai Univ, Fe
2O
3Provide by Nan Shangle chemical plant, Beijing, with 0.4989 gram indium nitrate crystal (In (NO
3)
3) 4.5H
2O) be dissolved in the 5ml deionized water, add 3.0 gram HZSM5 and 1.2 gram Fe again
2O
3Mixture, after fully stirring, left standstill 24 hours, 120 ℃ of bakings 3 hours place 700 ℃ of roastings of muffle furnace 4 hours, before the reaction, with the catalyst compressing tablet, break that to sieve out 30～60 purpose particles standby into pieces.
Embodiment 2 is microwave catalysis reduction nitric oxide under a large amount of oxygen existence conditions
Here only to contain indium 5% (weight percentage), the weight ratio of molecular sieve and iron oxide is 10: 4 In/HZSM5+Fe
2O
3(silica alumina ratio is 25) describes the active testing of microwave catalyst in the reaction of microwave catalysis reduction nitric oxide among the present invention prevailingly for example.Microwave catalysis device required in the test is made of microwave generator, annular device, waveguide, resonator and short-circuit plunger.Active testing carries out in fixed bed reactors.Reactor places in the resonator, perpendicular to magnetic direction, is parallel to direction of an electric field.Before advancing reactor, nitric oxide, methane, oxygen and helium fully mix in blender, catalyst amount 0.5 gram in the active testing, and unstripped gas air speed (GHSV) is 3600h
-1, reaction pressure is a normal pressure.Reaction temperature is measured with highly sensitive infrared radiation thermometer.With online chromatography analysis product, catalyst activity is a standard with the conversion ratio (%) that nitric oxide is converted into nitrogen.
The microwave catalysis reactivity of embodiment 3 different catalysts
| Catalyst I n/HZSM5 In/HZSM5+Ni 2O 3?In/HZSM5+Co 3O 4?In/HZSM5+Fe 2O 3Conversion ratio 0 72.2 90.0 100 |
In％＝5％，[HZSM5]∶[MxOy]＝10∶4，GHSV＝3600h
-1，
NO=2500ppm, CH4=2000ppm, O
2=4.0%, He is a balance gas, catalyst loading amount 1.0ml, and reaction pressure is a normal pressure, 40 watts of microwave powers.The content and the reaction temperature of embodiment 4 microwave carriers
To 5%In/HZSM5+Fe
2O
3The influence of microwave catalyst activity
| ??HZSM5： ??Fe 2O 3(weight ratio) | Reaction temperature (℃) * |
| ?????190??200??220??240??260??280??300 | |
| ????10∶4 ????10∶6 ????10∶8 | ??????????63.1?100??100??100??96.3?89.2 62.6??????100??100??92.0?85.0?77.3 ?????100??96.6?84.6?77.0 |
NO=2500ppm, CH4=2000ppm, O
2=4.0%, He is a balance gas,
GHSV=3600h
-1, catalyst loading amount 1.0ml, reaction pressure is a normal pressure,
*Reaction temperature is measured by infrared radiation thermometer.Embodiment 5 oxygen concentrations are to 5%In/HZSM5+Fe
2O
3The influence of (10: 4) microwave catalyst activity
| Unstripped gas air speed (h -1) | Reaction temperature (℃) * |
| ????200????220????240????260??280???300 |
| ??3600 ??7200 ??10800 | ??63.1??100?????100????100??96.3??89.2 ??62.6??85.2????100????100??98.3??84.6 ??65.2??84.7????100????100??94.7??83.5 |
NO=2500ppm, CH4=2000ppm, He are balance gas,
Catalyst loading amount 1.0ml, reaction pressure is a normal pressure,
*Reaction temperature is measured by infrared radiation thermometer.
Claims (3)
1. catalyst for eliminating nitrogen oxide by means of microwave catalysis, it is characterized in that: first active component of this catalyst is an indium, be supported on the natural or artificial synthetic molecular sieve, the silica alumina ratio of molecular sieve is less than 50, and the weight percentage of molecular sieve supported indium is 0.5～20%; It is higher to add dielectric constant, and the absorbing material of high temperature oxidation resisting is as microwave carrier, and this kind carrier is chosen as iron oxide, and iron is second active component of this catalyst, and the weight ratio of molecular sieve and iron oxide is 10: 0.5～10: 20.
2. the preparation method of the described catalyst for eliminating nitrogen oxide by means of microwave catalysis of claim 1 is characterized in that: catalyst is by the indium salt In (NO with solubility
3)
3Or InCl
3Adopt infusion process to make with the mixture of molecular sieve and iron oxide, or with In
2O
3Adopt mechanical mixing to make 550～900 ℃ of sintering temperatures, 3～6 hours time with the mixture of molecular sieve and iron oxide.
3. the described catalyst of claim 1 is used for eliminating oxynitrides under the microwave condition, and the reactor of use is parallel to direction of an electric field perpendicular to magnetic direction, and reaction temperature is between 150～600 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98114335A CN1095402C (en) | 1998-09-23 | 1998-09-23 | Catalyst for eliminating nitrogen oxide by means of microwave catalysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98114335A CN1095402C (en) | 1998-09-23 | 1998-09-23 | Catalyst for eliminating nitrogen oxide by means of microwave catalysis |
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| Publication Number | Publication Date |
|---|---|
| CN1248490A true CN1248490A (en) | 2000-03-29 |
| CN1095402C CN1095402C (en) | 2002-12-04 |
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ID=5224006
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98114335A Expired - Fee Related CN1095402C (en) | 1998-09-23 | 1998-09-23 | Catalyst for eliminating nitrogen oxide by means of microwave catalysis |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102489152A (en) * | 2011-12-30 | 2012-06-13 | 湘潭大学 | Denitration method by microwave catalytic reaction for direct decomposition of NO |
| CN104258866A (en) * | 2014-10-13 | 2015-01-07 | 河北科技大学 | Preparation method and application of microwave catalyst |
| CN108187732A (en) * | 2017-12-12 | 2018-06-22 | 哈尔滨工业大学深圳研究生院 | A kind of CH of sulfur resistive water resistant4SCR denitration and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE7538372U (en) * | 1975-12-02 | 1976-04-01 | Interatom Internationale Atomreaktorbau Gmbh, 5060 Bensberg | DEVICE FOR REPLACING CRUCIBLES IN A GLUEHOFEN |
| DE69026054T2 (en) * | 1989-12-28 | 1996-10-02 | Mitsubishi Heavy Ind Ltd | Denitrification catalyst for high temperature exhaust gases |
| RU2072897C1 (en) * | 1994-07-18 | 1997-02-10 | Институт катализа им.Г.К.Борескова СО РАН | Catalyst for removing nitrogen oxides from exhaust gases and method of preparation thereof |
| CN1179353A (en) * | 1996-10-16 | 1998-04-22 | 中国科学院金属研究所 | Microwave purifying catalyst for automobile tail gas |
-
1998
- 1998-09-23 CN CN98114335A patent/CN1095402C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102489152A (en) * | 2011-12-30 | 2012-06-13 | 湘潭大学 | Denitration method by microwave catalytic reaction for direct decomposition of NO |
| CN102489152B (en) * | 2011-12-30 | 2014-05-21 | 湘潭大学 | Denitration method by microwave catalytic reaction for direct decomposition of NO |
| CN104258866A (en) * | 2014-10-13 | 2015-01-07 | 河北科技大学 | Preparation method and application of microwave catalyst |
| CN104258866B (en) * | 2014-10-13 | 2018-08-31 | 河北科技大学 | A kind of preparation method and applications of microwave catalyst |
| CN108187732A (en) * | 2017-12-12 | 2018-06-22 | 哈尔滨工业大学深圳研究生院 | A kind of CH of sulfur resistive water resistant4SCR denitration and preparation method thereof |
| CN108187732B (en) * | 2017-12-12 | 2021-04-02 | 哈尔滨工业大学深圳研究生院 | Anti-sulfur and water-resistant CH4-SCR denitration catalyst and preparation method thereof |
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| Publication number | Publication date |
|---|---|
| CN1095402C (en) | 2002-12-04 |
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