CN1390634A - Plasma discharge reactor having multiple rotary disk electrodes with more tips - Google Patents
Plasma discharge reactor having multiple rotary disk electrodes with more tips Download PDFInfo
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- CN1390634A CN1390634A CN 02100881 CN02100881A CN1390634A CN 1390634 A CN1390634 A CN 1390634A CN 02100881 CN02100881 CN 02100881 CN 02100881 A CN02100881 A CN 02100881A CN 1390634 A CN1390634 A CN 1390634A
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Abstract
A plasma discharging reactor with rotating electrode is composed of cylindrical casing, fixed cylindrical electrode in the casing, and rotating electrode. Said rotating electrode has multiple multi-tip concentric disks fixed to it, the top end extended out of the casing and driven by drive mechanism, and the lower end in the recess of metallic base connected to high-voltage power supply. Its advantages are high conversion rate of methane (55-75%), high output rate of C2 hydrocarbon (45-70%) and high selectivity of C2 hydrocarbon (more than 95%).
Description
Technical field
The present invention relates to a kind of plasma discharge reactor having of a plurality of disk rotating electrodes of multi-stylus end.The innovative technology that belongs to plasma discharge reactor having,
Background technology
Along with the shortage day by day of petroleum resources, people more and more pay attention to the development and use of the big reserves energy gas in the world.Methane (CH
4) be the major ingredient of Sweet natural gas.Because CH
4Molecule has very high stability, uses CH
4Direct coupling system C
2Hydrocarbon (ethane, ethene, acetylene) is very disadvantageous on thermodynamics, adopts the direct coupling of conventional catalysis means not make a breakthrough always, and the plasma discharge reaction is for CH
4Coupling is a kind of very effective method, has become the interdisciplinary forward position research of physical chemistry focus in recent years.Plasma discharge reactor having is CH under the plasmoid
4Link coupled gordian technique, the electrode of this reactor are again key parts.The electrode of existing plasma discharge reactor having is by upper prong and the following flat fixed electorde that constitutes mostly, kind electrode is because electrical discharge zone electric field energy skewness, local energy density is excessive, forms a large amount of carbon distributions in reactor, to such an extent as to can't operate continuously.And because its reactant gas flow direction is parallel with direction of an electric field, have only partial reaction gas by reaction zone, capacity usage ratio is very low.A kind of upper knife edge rotating electrode of report and the plasma reactor of dull and stereotyped fixed electorde recently down, its electrode discharge is the discharge of swimming type on blade, rather than on whole blade, discharge, thereby discharge is a narrow regional area discharge, and this regional area discharge is always ceaselessly moved along blade, its actual effect still is equivalent to the discharge of the fixed electorde of upper prong and following slab construction, still can form a large amount of carbon distributions during discharge and can not operate continuously.And its CH
4Per pass conversion is the highest to have only 22.5%, corresponding C
2The hydrocarbon yield has only 15.2%.They all are difficult to realize industrialization.
Summary of the invention
The objective of the invention is to propose a kind of plasma discharge reactor having of a plurality of disk rotating electrodes of multi-stylus end.This reactor has CH
4Per pass conversion and C
2Hydrocarbon once through yield height, energy consumption is lower, and the few characteristics of carbon distribution.
In order to achieve the above object, the present invention is realized by following technical proposals: mainly by insulation barrel-type casing, the intravital tubular fixed electorde of shell and the plasma discharge reactor having that rotating electrode constituted by a plurality of disks of the multi-stylus end of driving mechanism driven rotary.It is characterized in that rotating electrode is a metal cylinder, fixedly connected concentrically ringed rosette is covered with float tooth cusp on the cylinder on the disk border, and stretch out outside the reactor upper end of metal cylinder, and link to each other with driving mechanism by insulating bar.Its lower end is connected with the rotation slot of the metab that is arranged on the interior bottom of housing.The overhanging metallic rod that this metab connected links to each other with high-voltage power supply one end.Rosette on the fixed electorde of tubular and the rotating electrode keeps concentric setting.
The material of above-mentioned metal cylinder and the rosette on it is copper, titanium, stainless steel, copper alloy and titanium alloy.
At least fixedly connected two concentrically ringed metal tip disks on the above-mentioned metal cylinder.
The disk outer rim of above-mentioned rotating electrode and the concentric(al) circles fixedly circular clearance of cylindrical electrode are 2～500mm.
The present invention compares with existing plasma discharge reactor having, has transformation efficiency, yield height and the few characteristics of carbon distribution.The methane per pass conversion can reach 55～75%, C
2The hydrocarbon once through yield can reach 45～70%, C
2Hydrocarbon-selective can reach more than 95%.
Description of drawings
Accompanying drawing is a structural representation of the present invention.
1 is the isolating joint of rotating electrode among the figure, and 2,8 is the sealing cover of housing, and 3 is housing, 4 is the leading-out end of fixed electorde, and 5 are the tail gas outlet, and 6 is the metab of rotating electrode, 7 is the external part of metab, and 9 is multi-stylus end rosette, and 10 are the reaction gas inlet.
Embodiment
In conjunction with the accompanying drawings the present invention is described as follows: reactor insulation shell internal diameter is 11～1010mm among the figure.The spacing of a plurality of conjuncted concentric discs on the housing internal rotation electrode column is more than the 10mm, column diameter 3～50mm, and disk diameter 5～10mm, thickness 1～5mm has a plurality of crowns on the disk border, tooth depth 1～20mm, the number of teeth is more than 4.Experiment flow mainly comprises gas flow control, electrode rotation control, high-voltage power supply, digital oscilloscope and gas chromatographic analysis five parts.Reactant gases CH
4And H
2Flow divide two-way to pass through mass flow controller and show, mix by Flow Measurement Display Meter after, enter gas chromatograph and reactor in succession.In the reaction process, reactant gases almost all passes through region of discharge continuously.High-voltage power supply adopts the AC/DC type of development voluntarily, operating frequency 20kHz, and output rating is adjustable continuously between 0～300w.When showing the gas purity enter reactor, gas chromatographic analysis reaches 98% when above, open rotating electrode control power supply and high-voltage power supply, by voltate regulator boosted voltage gradually from low to high, exchange or volts DS when reaching gas breakdown voltage when passing to, reactant gases begins discharge, and electric discharge phenomena are reactant gases that vertical current is crossed direction of an electric field forms homogeneous and bright between the two poles of the earth peripheral plasma reaction zone.Noiseless during discharge.Reaction end gas is taken a sample through six-way valve, do the qualitative and quantitative analysis of online TCD with the 102 type gas chromatographs that analytical instrument factory in Shanghai produces, use GDX-502 (60-80 order) chromatographic column (stainless steel coil pipe φ 2 * 4000) and C-R3A chromatographic data processor to provide color atlas.Chromatographic run condition: carrier gas H
2Press 1.5kPa, bridge electric current 150mA, column temperature and detected temperatures 313K before (＞99%), post.When methane and hydrogen feed mol ratio be 1: 1, when power input is 50～90w, the average per pass conversion of methane is 65%, C
2The average once through yield of hydrocarbon is 63%.Under above-mentioned methane and hydrogen feed mol ratio condition, the change feed flow rates is 40～120ml/min, and then power input changes scope at 86～90w, and the corresponding average per pass conversion of methane is 53～74%, C
2The average once through yield of hydrocarbon is 53～70%.
Claims (4)
1, a kind of plasma discharge reactor having of a plurality of disk rotating electrodes of multi-stylus end, this reactor is mainly by the insulation barrel-type casing, the intravital tubular fixed electorde of shell and the rotating electrode by a plurality of disks of the multi-stylus end of driving mechanism driven rotary are constituted, it is characterized in that: rotating electrode is a metal cylinder, fixedly connected concentrically ringed rosette on the cylinder, be covered with float tooth cusp on the disk border, stretch out outside the reactor upper end of metal cylinder, and link to each other with driving mechanism by insulating bar; Its lower end is connected with the rotation slot of the metab that is arranged on the interior bottom of housing, and the overhanging metallic rod that this metab connected links to each other with high-voltage power supply one end; Rosette on the fixed electorde of tubular and the rotating electrode keeps concentric setting.
2, by the plasma discharge reactor having of a plurality of disk rotating electrodes of the described multi-stylus end of claim 1, it is characterized in that: the material of metal cylinder and the rosette on it is copper, titanium, stainless steel, copper alloy and titanium alloy.
3, the plasma discharge reactor having by a plurality of disk rotating electrodes of the described multi-stylus end of claim 1 is characterized in that: fixedly connected at least two concentrically ringed metal tip disks on the metal cylinder.
4, by the plasma discharge reactor having of a plurality of disk rotating electrodes of the described multi-stylus end of claim 1, it is characterized in that: the disk outer rim of rotating electrode and the concentric(al) circles fixedly circular clearance of cylindrical electrode are 2～500mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021008817A CN1172884C (en) | 2002-02-07 | 2002-02-07 | Plasma discharge reactor having multiple rotary disk electrodes with more tips |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021008817A CN1172884C (en) | 2002-02-07 | 2002-02-07 | Plasma discharge reactor having multiple rotary disk electrodes with more tips |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1390634A true CN1390634A (en) | 2003-01-15 |
| CN1172884C CN1172884C (en) | 2004-10-27 |
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|---|---|---|---|
| CNB021008817A Expired - Fee Related CN1172884C (en) | 2002-02-07 | 2002-02-07 | Plasma discharge reactor having multiple rotary disk electrodes with more tips |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100368073C (en) * | 2005-03-14 | 2008-02-13 | 大连理工大学 | Atomospheric pressure glow discharge plasma reactor possessing rotary relix electrode |
| CN101219771B (en) * | 2008-01-18 | 2010-06-02 | 中国科学院广州能源研究所 | Plasma diffraction electrode |
| CN101752170B (en) * | 2010-02-01 | 2012-03-21 | 北京航空航天大学 | Discharging electrode of combined type discharging plasma reactor and method for regulating structure thereof |
| RU2466977C1 (en) * | 2011-04-01 | 2012-11-20 | Учреждение Российской академии наук Институт химии нефти Сибирского отделения РАН (ИХН СО РАН) | Method of obtaining c2+ -hydrocarbons from methane |
| CN103025039A (en) * | 2012-11-30 | 2013-04-03 | 大连理工大学 | Atmospheric pressure non-thermal plasma generator |
| CN103190203A (en) * | 2010-12-28 | 2013-07-03 | 株式会社小金井 | Ion generation device |
| CN105478240A (en) * | 2014-09-16 | 2016-04-13 | 孙红梅 | Electric discharging device of rotation electrode |
| CN106185806A (en) * | 2016-07-01 | 2016-12-07 | 中国科学院电工研究所 | A kind of device and method utilizing plasma-converted methane |
| CN108888269A (en) * | 2018-04-19 | 2018-11-27 | 南京邮电大学 | A kind of electrical impedance imaging electrode physical model device |
| CN109621715A (en) * | 2019-01-02 | 2019-04-16 | 浙江大学 | A kind of sliding arc plasma organic processing unit in conjunction with catalyst |
| CN110292896A (en) * | 2018-03-23 | 2019-10-01 | 中国科学技术大学 | A kind of preparation method of plasma reaction device and unsaturated hydrocarbons |
| CN113877384A (en) * | 2021-09-27 | 2022-01-04 | 华中科技大学 | High-power plasma gas purification device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100434406C (en) * | 2006-04-10 | 2008-11-19 | 天津大学 | Apparatus and method for converting natural gas into carbon dioxide by low-temperature plasma technology |
-
2002
- 2002-02-07 CN CNB021008817A patent/CN1172884C/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100368073C (en) * | 2005-03-14 | 2008-02-13 | 大连理工大学 | Atomospheric pressure glow discharge plasma reactor possessing rotary relix electrode |
| CN101219771B (en) * | 2008-01-18 | 2010-06-02 | 中国科学院广州能源研究所 | Plasma diffraction electrode |
| CN101752170B (en) * | 2010-02-01 | 2012-03-21 | 北京航空航天大学 | Discharging electrode of combined type discharging plasma reactor and method for regulating structure thereof |
| CN103190203A (en) * | 2010-12-28 | 2013-07-03 | 株式会社小金井 | Ion generation device |
| RU2466977C1 (en) * | 2011-04-01 | 2012-11-20 | Учреждение Российской академии наук Институт химии нефти Сибирского отделения РАН (ИХН СО РАН) | Method of obtaining c2+ -hydrocarbons from methane |
| CN103025039A (en) * | 2012-11-30 | 2013-04-03 | 大连理工大学 | Atmospheric pressure non-thermal plasma generator |
| CN105478240A (en) * | 2014-09-16 | 2016-04-13 | 孙红梅 | Electric discharging device of rotation electrode |
| CN106185806A (en) * | 2016-07-01 | 2016-12-07 | 中国科学院电工研究所 | A kind of device and method utilizing plasma-converted methane |
| CN106185806B (en) * | 2016-07-01 | 2018-07-31 | 中国科学院电工研究所 | A kind of device and method using plasma-converted methane |
| CN110292896A (en) * | 2018-03-23 | 2019-10-01 | 中国科学技术大学 | A kind of preparation method of plasma reaction device and unsaturated hydrocarbons |
| CN110292896B (en) * | 2018-03-23 | 2020-10-27 | 中国科学技术大学 | Plasma reaction device and preparation method of unsaturated hydrocarbon |
| CN108888269A (en) * | 2018-04-19 | 2018-11-27 | 南京邮电大学 | A kind of electrical impedance imaging electrode physical model device |
| CN109621715A (en) * | 2019-01-02 | 2019-04-16 | 浙江大学 | A kind of sliding arc plasma organic processing unit in conjunction with catalyst |
| CN113877384A (en) * | 2021-09-27 | 2022-01-04 | 华中科技大学 | High-power plasma gas purification device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1172884C (en) | 2004-10-27 |
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