CN102277214A - Gas catalysis integrated system - Google Patents
Gas catalysis integrated system Download PDFInfo
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- CN102277214A CN102277214A CN2010101999490A CN201010199949A CN102277214A CN 102277214 A CN102277214 A CN 102277214A CN 2010101999490 A CN2010101999490 A CN 2010101999490A CN 201010199949 A CN201010199949 A CN 201010199949A CN 102277214 A CN102277214 A CN 102277214A
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- far infrared
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- vibrator
- mixing device
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Abstract
The invention discloses a gas catalysis integrated system, comprising a far infrared vibrator, a catalytic cracking synthesizer and a gas agent mixing device. The far infrared vibrator consists of far infrared ceramic balls and magnetic high magnetic mineralizers; the catalytic cracking synthesizer consists of a precious metal oxidation material or a porous rare earth ceramic material. The gas agent mixing device is given a pulse signal by a magnetic turnover panel liquidometer, and a frequency converter receives the signal and controls a liquid feeding pump to charge liquid. Fuel gas of the gas catalysis integrated system can be loaded in a bottle for usage. The far infrared vibrator can emit far infrared with a certain frequency and wavelength and high magnetic field to break large gas cluster body into small cluster body molecular groups and part of a carbon chain is cut out, so the gas has substantially reduced affinity, substantially raised dissociating property and a reduced burning-point. The catalytic cracking synthesizer has dehydrogenation effect on the gas to avoid polymerization of small molecular groups. The gas agent mixing device can well mix the refined small molecular groups and a catalysis auxiliary agent to realize fully combustion, so as to increase a gas combustion speed and a flame temperature, and save gas.
Description
Technical field
The present invention relates to a kind of combustion gas catalysis integrated system.
Background technology
Fuel gas is developed greatly in the China that is applied in of industrial circle, especially tempo is exceedingly fast aspect industrial combustion, because most enterprises all adopt extensive traditional combustion mode, problems such as fuel gas buring is incomplete in combustion processes, flame temperature is low are more outstanding, not only cause the combustion gas waste, and cause environmental pollution.This combustion gas catalysis integrated system can make the refinement of combustion gas molecular grouping, catalysis, synergy, thereby improves the combustion utilization efficiency of combustion gas, saves combustion gas, reduces and pollute.
Summary of the invention
In order to overcome the deficiencies in the prior art, the object of the invention is to provide a kind of combustion gas catalysis integrated system.
The present invention is achieved through the following technical solutions:
A kind of combustion gas catalysis integrated system is by the far infrared rays vibrator, the catalytic cracking synthesizer, gas agent mixing device is formed, described far infrared rays vibrator is made up of far-infrared ray ceramic ball and high magnetic mineralizer, the catalytic cracking synthesizer is made up of precious metal oxidation material or porous rare earth stupalith, described gas agent mixing device is by the given pulse signal of magnetic turnover panel liquidometer, after frequency transformer receives signal, control fluid filling pump filling liquid, the use of can bottling of described combustion gas catalysis integrated system synthetic fuel gas, the far infrared rays vibrator can be launched the far infrared rays and the high high-intensity magnetic field of certain frequency and wavelength, the big cluster body of combustion gas molecular grouping is dispersed as little cluster body molecular grouping, carbochain partly is cut off, avidity reduces greatly, its free property improves greatly, and burning-point reduces; The catalytic cracking synthesizer plays the effect of dehydrogenation to combustion gas, makes subset that polymerization not take place; Gas agent mixing device can make subset can access fully synthetic and absorption the subset and the catalyst aid uniform mixing of refinement, and fully burning improves the combustionvelocity of combustion gas in combustion processes, promotes flame temperature, saves combustion gas.High energy fuels gas after synthetic can be filled in the steel cylinder and use, and compares with unstripped gas, saves combustion gas more than 50%.
The far infrared rays vibrator is made up of with the material that can launch high high-intensity magnetic field material that can be emitting far-infrared; The catalytic cracking synthesizer is made up of precious metal oxidation material or porous rare earth stupalith; Gas agent mixing device is made up of inlet pipe, decollator, mixing tank etc., gas enters from inlet pipe bottom in the mixing tank and the catalyst aid uniform mixing, filler is housed in the mixing tank, use as transfer medium, gas liquid mixture realizes that with the gas of by-pass line secondary mixes, be provided with snubber assembly in the mixing tank air outlet, reduce the flow velocity of combustion gas, the gas that mixes after finishing is exported through exhaust line.Set in advance the liquid level difference of magnetic turnover panel liquidometer, when liquid is lower than preset value, the pulse signal of liquidometer transmitter output 4~20mA, frequency-variable controller receives pulse signal, control fluid filling pump quantitative liquid feeding.
Fuel gas enters the far infrared rays vibrator by the position of inlet mouth (4), and gas is during by far infrared rays and high magnetic refinement material, and big cluster body molecular grouping is dispersed as little cluster body molecular grouping; Little cluster body molecular grouping enters the catalytic cracking synthesizer by path (5) and (6), and little cluster body molecular grouping effectively carries out dehydrogenation reaction under the katalysis of precious metal oxidation material, thereby makes little cluster body molecular grouping that polymerization not take place; Path (7) and (8) that little cluster body molecular grouping passes through, enter gas agent mixing device, with catalyst aid thorough mixing, absorption, regulate gas agent ratio through bypass (10) control valve, gas arrives in the top exit snubber and mixes once more, the high energy fuels gas that mixes is transported to the terminal burner and uses through air outlet (9) output, also can use in overdraft is filled into steel cylinder.
Combustion gas catalysis integrated system is installed on the steel base, the external 220V power supply of fluid filling pump, and the power supply access way adopts explosion-proof processing, and integrated system is furnished with carbon steel sheet system tr, prevents rain erosion.
The invention has the beneficial effects as follows:
The far infrared rays vibrator can be launched the far infrared rays and the high high-intensity magnetic field of certain frequency and wavelength, and the big cluster body of combustion gas molecular grouping is dispersed as little cluster body molecular grouping, and carbochain partly is cut off, and avidity reduces greatly, and its free property improves greatly, burning-point reduces; The catalytic cracking synthesizer plays the effect of dehydrogenation to combustion gas, makes subset that polymerization not take place; Gas agent mixing device can be fully burned the subset and the catalyst aid thorough mixing of refinement in combustion processes, improve the combustionvelocity of combustion gas, promotes flame temperature, saves combustion gas.
Description of drawings
The invention will be further described below in conjunction with the drawings and specific embodiments.
Fig. 1 is a structural representation of the present invention.
Embodiment
With reference to Fig. 1, a kind of combustion gas catalysis integrated system, it is characterized in that: by far infrared rays vibrator (1), catalytic cracking synthesizer (2), gas agent mixing device (3) is formed, described far infrared rays vibrator (1) is made up of far-infrared ray ceramic ball and high magnetic mineralizer, catalytic cracking synthesizer (2) is made up of precious metal oxidation material or porous rare earth stupalith, described gas agent mixing device (3) is by the given pulse signal of magnetic turnover panel liquidometer, after frequency transformer receives signal, control fluid filling pump filling liquid, the use of can bottling of described combustion gas catalysis integrated system synthetic fuel gas, described far infrared rays vibrator (1) is provided with inlet mouth (4), be respectively arranged with air outlet (9) on the described gas agent mixing device (3) and add agent mouth (32), fuel gas enters the far infrared rays vibrator by the position of inlet mouth (4), gas is during by far infrared rays and high magnetic refinement material, and big cluster body molecular grouping is dispersed as little cluster body molecular grouping; Little cluster body molecular grouping enters the catalytic cracking synthesizer by path (5) and (6), and little cluster body molecular grouping effectively carries out dehydrogenation reaction under the katalysis of precious metal oxidation material, thereby makes little cluster body molecular grouping that polymerization not take place; Little cluster body molecular grouping enters gas agent mixing device by path (7) and (8), with catalyst aid thorough mixing, absorption, regulate gas agent ratio through bypass (10) control valve, gas arrives in the top exit snubber and mixes once more, the high energy fuels gas that mixes is exported through air outlet (9), be transported to the terminal burner and use, also can in overdraft is filled into steel cylinder, use.
In addition, the present invention is not limited to above-mentioned embodiment, as long as it reaches technique effect of the present invention with essentially identical means, all should belong to protection scope of the present invention.
Claims (4)
1. combustion gas catalysis integrated system, it is characterized in that: form by far infrared rays vibrator (1), catalytic cracking synthesizer (2), gas agent mixing device (3), described far infrared rays vibrator (1) is made up of infrared ceramic ball and high magnetic mineralizer, catalytic cracking synthesizer (2) is made up of precious metal oxidation material or porous rare earth stupalith, described gas agent mixing device (3) is by the given pulse signal of magnetic turnover panel liquidometer, after frequency transformer receives signal, control fluid filling pump filling liquid.
2. a kind of combustion gas catalysis integrated system according to claim 1 is characterized in that the use of can bottling of described combustion gas catalysis integrated system synthetic fuel gas.
3. a kind of combustion gas catalysis integrated system according to claim 1 is characterized in that described far infrared rays vibrator (1) is provided with inlet mouth (4).
4. a kind of combustion gas catalysis integrated system according to claim 1 is characterized in that being respectively arranged with on the described gas agent mixing device (3) air outlet (9) and adds agent mouth (32).
Priority Applications (1)
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CN2010101999490A CN102277214A (en) | 2010-06-10 | 2010-06-10 | Gas catalysis integrated system |
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CN2010101999490A CN102277214A (en) | 2010-06-10 | 2010-06-10 | Gas catalysis integrated system |
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CN2010101999490A Pending CN102277214A (en) | 2010-06-10 | 2010-06-10 | Gas catalysis integrated system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105482855A (en) * | 2016-01-26 | 2016-04-13 | 四川复力环保科技有限公司 | Fuel oil processing method and generator |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2546510Y (en) * | 2002-05-16 | 2003-04-23 | 徐秋桃 | Clear and energy-saving full-automatic water supply device |
CN101314128A (en) * | 2007-05-31 | 2008-12-03 | 中国科学院大连化学物理研究所 | Self-heating reforming hydrogen production catalyst and preparation method thereof |
CN201195720Y (en) * | 2008-04-11 | 2009-02-18 | 包头葳特冶金化学科技发展有限公司 | Rare earth activation gas energy conservation synergistic device |
CN201482470U (en) * | 2009-05-26 | 2010-05-26 | 周民智 | Molecule catalytic converter |
-
2010
- 2010-06-10 CN CN2010101999490A patent/CN102277214A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2546510Y (en) * | 2002-05-16 | 2003-04-23 | 徐秋桃 | Clear and energy-saving full-automatic water supply device |
CN101314128A (en) * | 2007-05-31 | 2008-12-03 | 中国科学院大连化学物理研究所 | Self-heating reforming hydrogen production catalyst and preparation method thereof |
CN201195720Y (en) * | 2008-04-11 | 2009-02-18 | 包头葳特冶金化学科技发展有限公司 | Rare earth activation gas energy conservation synergistic device |
CN201482470U (en) * | 2009-05-26 | 2010-05-26 | 周民智 | Molecule catalytic converter |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105482855A (en) * | 2016-01-26 | 2016-04-13 | 四川复力环保科技有限公司 | Fuel oil processing method and generator |
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Application publication date: 20111214 |