CN110127601A - The method of reaction of low temperature plasma equipment and decomposing hydrogen sulfide - Google Patents
The method of reaction of low temperature plasma equipment and decomposing hydrogen sulfide Download PDFInfo
- Publication number
- CN110127601A CN110127601A CN201810136025.2A CN201810136025A CN110127601A CN 110127601 A CN110127601 A CN 110127601A CN 201810136025 A CN201810136025 A CN 201810136025A CN 110127601 A CN110127601 A CN 110127601A
- Authority
- CN
- China
- Prior art keywords
- reaction
- inner cylinder
- low temperature
- temperature plasma
- grounding electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J19/088—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/02—Preparation of sulfur; Purification
- C01B17/04—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
- C01B17/0495—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by dissociation of hydrogen sulfide into the elements
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Abstract
The present invention relates to plasma chemistry fields, disclose the method for reaction of low temperature plasma equipment and decomposing hydrogen sulfide, which includes: inner cylinder (1)；Outer cylinder (2), the outer cylinder (2) are nested in the outside of the inner cylinder (1)；Central electrode (3), the central electrode are arranged in the inner cylinder (1)；The grounding electrode (4) for being formed and being formed at least partly side wall of inner cylinder by solid conductive material or be circumferentially positioned on the inner sidewall of inner cylinder；Block media between grounding electrode and central electrode is set.Reaction of low temperature plasma equipment provided by the invention can realize the lasting of hydrogen sulfide decomposable process and be stablized under significantly higher hydrogen sulfide conversion ratio and be carried out, and device can be realized long-term operation.
Description
Technical field
The present invention relates to plasma chemistry fields, and in particular to a kind of reaction of low temperature plasma equipment and a kind of decomposition
The method of hydrogen sulfide.
Background technique
Hydrogen sulfide (H2S it is) a kind of hypertoxic, stench sour gas, can not only causes the corrosion of the materials such as metal, but also
It can be detrimental to health, pollute environment.The large and medium-sized oil plant in China is all made of traditional Claus method (Claus) processing and contains at present
H2The tail gas of S, and Recovered sulphur.This method has only recycled the sulphur in hydrogen sulfide, but converts water for valuable hydrogen.From resource
It comprehensively utilizes angle and considers that in traditional hydrogen sulfide recovery process, hydrogen resource is not effectively utilized.Therefore, will
Hydrogen sulfide is decomposed into sulphur and hydrogen has been increasingly becoming the technical field that domestic and international researcher is paid close attention to.
Currently, hydrogen sulfide decomposition method specifically includes that high-temperature decomposition, electrochemical process, photocatalytic method and low-temperature plasma
Body method etc..In aforementioned a variety of methods, high temperature thermal decomposition method relative maturity in industrial technology, but hydrogen sulfide thermal decomposition is consumingly
Limited dependent on reaction temperature, and by thermodynamical equilibrium, though reaction temperature at 1000 DEG C or more, the conversion ratio of hydrogen sulfide
Only 20%.In addition, hot conditions are to the more demanding of reactor material, this also will increase operating cost.Further, since vulcanization
Hydrogen thermal decomposition conversion ratio is low, needs to separate a large amount of hydrogen sulfide gas from tail gas and recycle in systems, therefore also reduce
Unit efficiency and energy consumption is increased, these bring difficulty to its large industrialized application.Although using membrane technology can be with
Product is efficiently separated to break balance limitation, improves hydrogen sulfide conversion ratio, but thermal decomposition temperature tends to exceed the pole of film
Heat resisting temperature is limited, membrane material structure is destroyed.Electrochemistry rule there are operating procedures more, equipment seriously corroded, reaction are steady
The disadvantages of qualitative difference and low efficiency.Photocatalytic method decomposing hydrogen sulfide mainly uses for reference the research of photochemical catalyzing, research emphasis collection
In in terms of developing high efficiency semiconductor.Using solar energy come decomposing hydrogen sulfide, with low energy consumption, reaction condition temperature
It is relatively inexpensive method with simple operation and other advantages.But that there are treating capacities is small for this method, catalytic efficiency is low and is catalyzed
Agent is easy the problems such as inactivation.
Compared with other decomposition methods, low-temperature plasma body method has easy to operate, and device volume is small, and energy efficiency is high
The advantages that, and the reaction being directed to has the controllability of height, and it can be when small treating capacity, being difficult to focus on flexibly
It is applied on ground.Further, since it has the characteristics that high-energy density and can shorten the reaction time, can be realized at a lower temperature
Hydrogen sulfide is effectively decomposed, the changeable occasion of different scales, scattered distribution, working condition is suitable for.Moreover, recycling
While sulphur, hydrogen resource reclaim can be realized the utilization of hydrogen sulfide recycling by low-temperature plasma body method.
Currently, researchers at home and abroad conduct extensive research low temperature plasma decomposing hydrogen sulfide technology, use
Discharge type mainly include glow discharge, corona discharge, sliding arc discharge, microwave plasma, radio frequency plasma and
Dielectric barrier discharge etc..
Document " International journal of hydrogen energy ", 2012,37:1335-1347. use
The method decomposing hydrogen sulfide for shrinking normal glow discharge, is vulcanized under the conditions of pressure 0.02Mpa, 2000~4000K of temperature
The minimum decomposition energy consumption of hydrogen is 2.35eV/H2S.But this reaction temperature is high, pressure is low, and condition harshness is not easy to realize.
Document " International journal of hydrogen energy ", 2012,37:10010-10019 adopt
With microwave plasma decomposition hydrogen sulfide, hydrogen sulfide can be decomposed completely under the conditions of atmospheric pressure, temperature 2400K, but after decomposition
Hydrogen and sulphur can at high temperature rapidly it is compound regenerate hydrogen sulfide, there has been no corresponding quenching measures at present.
Document " Chemical Engineering Science ", 2009,64 (23): 4826-4834. uses impulse electric corona
Electric discharge has carried out H2S decomposes the research of hydrogen making and sulphur, and reactor uses line tubular structure, in constant power 100W condition
Under investigated pulse electric capacity, discharge voltage and pulse frequency to H2S conversion ratio and the influence for decomposing efficiency.As a result table
Bright, under conditions of power is certain, low pulse electric capacity, low discharge voltage and high pulse frequencies help to obtain high H2S
Decompose efficiency；In addition, with Ar and N2It is compared as Balance Air, with Ar-N2It is available higher when gaseous mixture is as Balance Air
H2S conversion ratio, in Ar/N2/H2When S volume fraction is 46%/46%/8%, discharge power 60W, pulse electric capacity 720pF,
The H of acquisition2The minimum decomposition energy consumption of S is 4.9eV/H2S, but H at this time2S conversion ratio is only 30% or so.In addition, this reaction system
Flow is only 1.18 × 10-4SCMs-1, this low discharge, low concentration, low-conversion reaction effect do not have in the industrial production
Practical significance.
Document " Journal of applied physics ", 1998,84 (3): 1215-1221 uses sliding arc discharge
To H2S decomposition reaction is studied, and method is by H2S Dilution air to concentration is 0~100ppm, in gas overall flow rate
To have investigated flow rate of gas, reaction cavity size and frequency under the conditions of 0~100L/min to H2The influence of S decomposition reaction.
The experimental results showed that low gas flow rate, shallow bid spacing and low frequency help to obtain higher H2S conversion ratio, in the electric discharge of optimization
Under the conditions of obtained H2S conversion ratio is up to 75~80%, but H2S decomposes energy consumption and is up to 500eV/H2S, this concentration is low, energy consumption is high
Reaction effect is also without prospects for commercial application.
Dielectric barrier discharge can usually generate under atmospheric pressure, and discharge temp is lower.Further, since the presence of medium
The growth of discharge current is limited, punctures completely so as to avoid gas and forms spark or electric arc, this is conducive to large volume, stabilization
The generation of plasma has preferable prospects for commercial application.
Document " Plasma chemistry and plasma processing ", 1992,12 (3): 275-285 use changes
Into ozone generator investigated H2Flash-over characteristic of the S within the scope of 130~560 DEG C, and have studied reaction temperature, H2S charging is dense
Degree, injecting power and addition H2、Ar、N2Deng to H2The influence of S conversion ratio and energy efficiency, experiment discovery addition Ar can promote
Into H2The decomposition of S, in 50~100mL/min of total flow, H2S concentration obtained under the conditions of being 20~100% conversion ratio be 0.5~
12%, most low yield Hydrogen Energy consumption is about 0.75mol/kWh (50eV/H2), however, this process still remains, conversion ratio is low and energy consumption is high
The shortcomings that.
CN102408095A cooperates with decomposing hydrogen sulfide using dielectric barrier discharge and photochemical catalyst, and method is that will have light
The solid catalyst of catalytic activity is filled in plasma slab, however this method is decomposed the sulphur generated there are hydrogen sulfide and can be deposited
The shortcomings that below catalyst bed.
Document " International Journal of Energy Research ", 2013,37 (11): 1280-1286.
By Al2O3, MoOx/Al2O3, CoOx/Al2O3And NiO/Al2O3Catalyst is filled in region of discharge, using dielectric barrier discharge and urges
Agent has carried out H2S decomposes research.Reaction result shows MoOx/Al2O3And CoOx/Al2O3Catalyst has better effects；Wherein
As filling MoOx/Al2O3Catalyst, in H2S/Ar total flow 150mL/min, H2S concentration is 5 volume %, injection ratio energy SIE is
When 0.92kJ/L, catalyst filling length are bed 10%, obtained H2S maximum conversion is about 48%.But this reaction process
Concentration of hydrogen sulfide is lower, decomposes the sulfur deposition of generation in inside reactor, with the extension of time, catalyst activity reduction,
Discharge stability reduces, and the conversion ratio of hydrogen sulfide is caused to gradually decrease.
The characteristics of CN103204466A discloses a kind of controlling temp type hydrogen sulfide decomposer and method, the device is middle electrocardio
Extremely metal, the circulating liquid that grounding electrode is temperature-controllable, are controlled by the temperature of liquid grounding electrode, so that hydrogen sulfide point
Solution preocess is capable of the progress of continuous-stable.In addition, CN103204467A, which discloses a kind of hydrogen sulfide, continually and steadily decomposes preparing hydrogen
The characteristics of device and method of gas, the prior art is the circulation fluid using central electrode as metal, grounding electrode for temperature-controllable
Body carries out temperature control by liquid grounding electrode, and raw material airintake direction is for circumferential air inlet and in a spiral mode along axial reverse
By region of discharge, so that the sulphur generated is come out by timely centrifuge separation.However, CN103204466A and CN103204467A is public
In order to guarantee that hydrogen sulfide is fully decomposed as far as possible in the method opened, the flow velocity for needing to control hydrogen sulfide makes it in reactor
Residence time in inner cylinder is longer and the size electric energy that the gas of unit volume in inner cylinder is obtained of control inner cylinder is more,
Also, since the current prior art can not provide more powerful power supply so that using CN103204466A and
Method disclosed in CN103204467A even control hydrogen sulfide residence time it is longer and control inner cylinder size so that
The electric energy that the gas of unit volume obtains in inner cylinder is more also merely capable of so that the maximum conversion of hydrogen sulfide reaches 20% left side
The right side, also, when the maximum conversion of hydrogen sulfide reaches 20% or so, the energy consumption for vulcanizing hydroperoxide decomposition reaction is quite high, and uncomfortable
Together in large scale industry application.Further, there is also available liquid in method disclosed in CN103204466A and CN103204467A
The few defect of the type of body grounding electrode, disclosed in salting liquid etc. to be generally only capable of maintaining the temperature of reactor be 100 DEG C
Hereinafter, and be easy to causeing the blocking of reactor hereinafter, elemental sulfur is generally solid-state at 100 DEG C.
Summary of the invention
The purpose of the invention is to the reaction of low temperature plasma equipment for overcoming the prior art to provide for hydrogen sulfide
Decomposition when existing hydrogen sulfide conversion ratio it is low and decompose the high defect of energy consumption, a kind of new hydrogen sulfide that can be improved is provided and is turned
Rate and the method for reducing the reaction of low temperature plasma equipment for decomposing energy consumption and application the consersion unit decomposing hydrogen sulfide.
To achieve the goals above, in a first aspect, the present invention provides a kind of reaction of low temperature plasma equipment, which is set
It is standby to have with shaft jacket core structure, and the consersion unit includes:
Inner cylinder is respectively arranged with reactant entrance and product exit on the inner cylinder；
Outer cylinder, the outer cylinder is nested in the outside of the inner cylinder, and heat-conducting medium entrance is respectively arranged on the outer cylinder
It is exported with heat-conducting medium；
Central electrode, the central electrode are arranged in the inner cylinder；
Grounding electrode, the material for forming the grounding electrode is solid conductive material, and the grounding electrode forms inner cylinder
At least partly side wall or the grounding electrode is circumferentially positioned on the inner sidewall of the inner cylinder；And
Block media, institute's block media are circumferentially positioned between the central electrode and the grounding electrode, and point
Be not all larger than with the distance between the central electrode and the grounding electrode 0 and the setting position of the block media make
The region of discharge between the central electrode and the grounding electrode is obtained by the block media interval；
Wherein, the distance between inner sidewall of the lateral wall of the central electrode and the grounding electrode is d1, Yi Jisuo
State block media with a thickness of D1, and L1=d1-D1, and L1With D1Proportionate relationship are as follows: L1: D1=(0.05~100): 1.
Second aspect, the present invention provide a kind of method of decomposing hydrogen sulfide, and this method is described in the first aspect present invention
Implement in reaction of low temperature plasma equipment, this method comprises: under the conditions of dielectric barrier discharge, by the raw material containing hydrogen sulfide
Gas carries out the decomposition reaction of hydrogen sulfide from the inner cylinder that reactant entrance is introduced to the reaction of low temperature plasma equipment, decomposes
The logistics obtained afterwards is drawn by the product exit, also, by continuing from heat-conducting medium entrance to the low temperature plasma
Heat-conducting medium is introduced in the outer cylinder of consersion unit and the heat-conducting medium is drawn by heat-conducting medium outlet and maintains the low temperature
Temperature needed for plasma reaction device；The dielectric barrier discharge is formed by grounding electrode, block media and central electrode.
The plasma that aforementioned reaction of low temperature plasma equipment provided by the invention can be used in hydrogen sulfide decomposes, this is anti-
It answers equipment that can generate uniform, efficient dielectric barrier discharge, generates hydrogen and sulphur so that hydrogen sulfide directly be decomposed.
Aforementioned reaction of low temperature plasma equipment provided by the invention is that the jacket type dielectric impedance with coaxial configuration is put
Electric consersion unit, basic structure mainly include central electrode, solid grounding electrode and block media etc., the telescoping structure energy
Enough so that heat-conducting medium carries out circulating-heating or cooling to discharging reaction equipment, to realize the flexible temperature control to region of discharge
System.Particularly, the present invention passes through control L1(the distance between lateral wall and the inner sidewall of grounding electrode of central electrode are d1,
And block media with a thickness of D1, and L1=d1-D1) with the thickness D of block media1Proportionate relationship are as follows: L1: D1=(0.05
~100): 1 and when applying solid grounding electrode, can improve compared with the existing technology significantly the conversion ratio of hydrogen sulfide with
And it reduces and decomposes energy consumption.
In addition, reaction of low temperature plasma equipment provided by the invention can be real under significantly higher hydrogen sulfide conversion ratio
Existing hydrogen sulfide decomposable process continues and stablizes to carry out, and device can be realized long-term operation.And it is provided by the invention
Reaction of low temperature plasma equipment can also be used to big flow, the hydrogen sulfide treatment process of high concentration.
Detailed description of the invention
Fig. 1 is that a kind of structure of preferred embodiment of reaction of low temperature plasma equipment provided by the invention is shown
It is intended to；
Fig. 2 is the structure of another preferred embodiment of reaction of low temperature plasma equipment provided by the invention
Schematic diagram.
Description of symbols
1, inner cylinder 2, outer cylinder
11, reactant entrance 21, heat-conducting medium entrance
12, product gas outlet 22, heat-conducting medium outlet
13, liquid product outlet
3, central electrode
4, grounding electrode
5, it is grounded
6, block media
Specific embodiment
The endpoint of disclosed range and any value are not limited to the accurate range or value herein, these ranges or
Value should be understood as comprising the value close to these ranges or value.For numberical range, between the endpoint value of each range, respectively
It can be combined with each other between the endpoint value of a range and individual point value, and individually between point value and obtain one or more
New numberical range, these numberical ranges should be considered as specific open herein.
As previously mentioned, the present invention provides a kind of reaction of low temperature plasma equipment, the reactions for the first aspect of the present invention
Equipment has with shaft jacket core structure, and the consersion unit includes:
Inner cylinder is respectively arranged with reactant entrance and product exit on the inner cylinder；
Outer cylinder, the outer cylinder is nested in the outside of the inner cylinder, and heat-conducting medium entrance is respectively arranged on the outer cylinder
It is exported with heat-conducting medium；
Central electrode, the central electrode are arranged in the inner cylinder；
Grounding electrode, the material for forming the grounding electrode is solid conductive material, and the grounding electrode forms inner cylinder
At least partly side wall or the grounding electrode is circumferentially positioned on the inner sidewall of the inner cylinder；And
Block media, the block media are circumferentially positioned between the central electrode and the grounding electrode, and respectively
With the distance between the central electrode and the grounding electrode be all larger than 0 and the setting position of the block media make
Region of discharge between the central electrode and the grounding electrode is by the block media interval；
Wherein, the distance between inner sidewall of the lateral wall of the central electrode and the grounding electrode is d1, Yi Jisuo
State block media with a thickness of D1, and L1=d1-D1, and L1With D1Proportionate relationship are as follows: L1: D1=(0.05~100): 1.
Difference between " side wall " and " lateral wall " and " inner sidewall " of the invention are as follows: " lateral wall " and " inner sidewall " difference
Indicate " side wall " outer surface and inner surface.
Under preferable case, L1: D1=(0.1~30): 1.
The jacket structured design of the invention, enables to heat-conducting medium to circulate in shell, is guaranteeing that electric discharge is strong
Entire consersion unit can be made to maintain in certain temperature range while spending, so that the sulphur generated is flowed out reaction in liquid form and set
It is standby, it can effectively avoid hydrogen sulfide from decomposing the sulphur solidification generated, this can be made to decompose while reaching higher conversion ratio
Cheng Chixu, stable realization long-term operation.
Under preferable case, the block media is fixedly connected with the top and/or bottom of the inner cylinder；It is highly preferred that described
One end that the inner cylinder is fixedly connected in block media is provided with pore structure, enables reactants and products in the inner cylinder
Entered or drawn by the pore structure.
There is no particular limitation for fixed form of the present invention to the block media, as long as enabling to the block media
It is fixedly connected on the top and/or bottom of the inner cylinder.
According to a kind of preferred embodiment, the number of the inner cylinder is 1.
According to another preferred embodiment, the number of the inner cylinder is 2 or more, and in each inner cylinder
It is respectively arranged with the central electrode, the grounding electrode and the block media.It is excellent in the preferred embodiment
In the case of choosing, each central electrode is connected in parallel；Preferably, each grounding electrode is connected in parallel.
Preferably, the material for forming the block media is electrically insulating material.It is highly preferred that forming the block media
Material is selected from least one of glass, ceramics, enamel, polytetrafluoroethylene (PTFE) and mica.The glass can for quartz glass or
Hard glass；The material for forming the block media can also be other metals and nonmetallic multiple with high voltage electrical isolation design
Condensation material etc..The ceramics can be aluminium oxide ceramics.
Preferably, which further includes ground line, described to be grounded the lateral wall that the outer cylinder is arranged in, and one end
It is connect with the grounding electrode.
Preferably, the top of the inner cylinder is arranged in the reactant entrance, and the product exit is arranged in the inner cylinder
Lower part and/or bottom.
According to a kind of preferred embodiment, the product exit includes that product gas outlet and product liquid go out
Mouthful, and the lower part of the inner cylinder is arranged in for the product gas outlet and the liquid product outlet is arranged in the inner cylinder
Bottom.
The internal diameter of the inner cylinder of the invention and the ratio between the aperture of the product exit can be (0.1~100): 1.
The aperture of the reactant entrance of the invention and the ratio between the aperture of the product exit can be (0.1~120):
1。
Ratio between the length of the inner cylinder of the invention and the internal diameter of the inner cylinder can be (0.5~500): 1.
Preferably, the product gas outlet is arranged in the lower section of the region of discharge, and the product gas outlet
Height H of the position relative to the inner cylinder bottom is set1With the length L of the region of discharge2Between proportionate relationship are as follows: H1: L2
=1:(0.05~25000)；Preferably H1: L2=1:(0.1~10000)；More preferably H1: L2=1:(0.5~1000).It is excellent
Selection of land, the heat-conducting medium entrance and heat-conducting medium outlet are separately positioned on the lower part and top of the outer cylinder.
In the present invention, to the internal diameter ratio between the inner barrel and outer barrel, there is no particular limitation, main in the inner cylinder
For occurring to vulcanize hydroperoxide decomposition reaction, and the outer cylinder is mainly used for providing required temperature for the decomposition reaction in inner cylinder, therefore,
Those skilled in the art can adjust according to the purposes and select the internal diameter ratio between suitable inner barrel and outer barrel.
The reactant entrance of the invention is arranged to the unstripped gas entered in the inner cylinder and the inner cylinder
Internal diameter it is parallel or at an angle, such as can be tangentially-arranged.
The internal diameter of the invention indicates diameter.
Preferably, the material for forming the grounding electrode is selected from graphite-pipe, metal tube, metal foil or metal mesh.The present invention
Solid grounding electrode, cooperate the structure of reaction of low temperature plasma equipment of the invention, under conditions of injecting power is certain
The micro discharge electric current of generation is bigger, is more advantageous to the scission of link decomposition reaction of hydrogen sulfide.It is formed in the material of the grounding electrode
Metal tube and metal foil may include elemental metals pipe, elemental metals foil, alloying metal pipe, alloying metal foil.Hair of the invention
Bright people's discovery, when being circumferentially positioned on the lateral wall of the inner cylinder using solid conductive material as grounding electrode, is enabled to
When carrying out vulcanization hydroperoxide decomposition reaction using reaction of low temperature plasma equipment provided by the invention, the conversion ratio of hydrogen sulfide is more significant
It improves on ground.
The material for forming the central electrode is conductive material, it is preferable that the material for forming the central electrode is selected from stone
At least one of Mo Guan, metal bar, metal tube and graphite rod.The metal bar, metal tube may include elemental metals stick, close
Golden metal bar, elemental metals pipe, alloying metal pipe.The material of the formation central electrode of the invention has and can have to be other
The rodlike and tubular material of electric conductivity.
The present invention can be introduced thermally conductive by the region between the lateral wall of the inner cylinder and the inner sidewall of the outer cylinder
Medium and the temperature for the consersion unit for having jacket structured is maintained between such as 119~444.6 DEG C, to guarantee hydrogen sulfide
It decomposes the sulphur generated and flows out region of discharge in liquid form.
Can also be filled in the reaction of low temperature plasma equipment of the invention can catalysed curing hydrogen resolve into list
The catalyst of matter sulphur and hydrogen, the catalyst are preferably seated in the consersion unit inner cylinder.The present invention is to the catalyst
Admission space and filling type do not require particularly, about the type of catalyst, for example, can for CN102408095A,
In catalyst disclosed in CN101590410A and CN103495427A any one or it is a variety of.
As previously mentioned, the second aspect of the present invention provides a kind of method of decomposing hydrogen sulfide, this method is in aforementioned first party
Implement in reaction of low temperature plasma equipment described in face, this method comprises: vulcanization will be contained under the conditions of dielectric barrier discharge
The unstripped gas of hydrogen carries out the decomposition of hydrogen sulfide from the inner cylinder that reactant entrance is introduced to the reaction of low temperature plasma equipment
Reaction, the logistics obtained after decomposition drawn by the product exit, also, by continuing from heat-conducting medium entrance to the low temperature
Heat-conducting medium is introduced in the outer cylinder of plasma reaction device and is drawn the heat-conducting medium by heat-conducting medium outlet and is maintained
Temperature needed for the reaction of low temperature plasma equipment, the dielectric barrier discharge is by grounding electrode, block media and center
Electrode is formed.
Item of the reaction of low temperature plasma equipment provided by the invention to decomposition reaction involved in decomposing hydrogen sulfide
Part is not particularly limited, and can be various involved in the plasma decomposing hydrogen sulfide method in the art routinely used
Condition is decomposed, and lists to the embodiment of the present invention exemplary partial the condition of decomposing hydrogen sulfide, those skilled in the art
Member should not be construed as limiting the invention.
In the present invention, to the material of the formation outer cylinder, there is no particular limitation, as long as forming the material of the outer cylinder
It is able to bear the set temperature of heat-conducting medium.
The reaction of low temperature plasma equipment provided by the invention is to the hydrogen sulfide in the gas at reactant entrance
There is no particular limitation for concentration, such as the concentration of hydrogen sulfide can be 0.01~100 volume % in gas.
A kind of preferred embodiment of reaction of low temperature plasma equipment of the invention is provided below in conjunction with Fig. 1
Structure, specifically:
The consersion unit has with shaft jacket core structure, and the consersion unit includes:
Inner cylinder 1 is respectively arranged with reactant entrance 11 and product exit on the inner cylinder 1；
Outer cylinder 2, the outer cylinder 2 is nested in the outside of the inner cylinder 1, and is respectively arranged with heat-conducting medium on the outer cylinder 2
Entrance 21 and heat-conducting medium outlet 22；
Central electrode 3, the central electrode 3 are arranged in the inner cylinder 1；
Grounding electrode 4, the material for forming the grounding electrode 4 is solid conductive material, and the grounding electrode 4 forms inner cylinder
1 at least partly side wall or the grounding electrode 4 is circumferentially positioned on the lateral wall of the inner cylinder 1；And
Block media 6, the block media 6 are circumferentially positioned between the central electrode 3 and the grounding electrode 4, and
The setting position of 0 and the block media is all larger than with the distance between the central electrode 3 and the grounding electrode 4 respectively
It sets so that the region of discharge between the central electrode and the grounding electrode is by the block media interval；
Wherein, the distance between inner sidewall of the lateral wall of the central electrode 3 and the grounding electrode is d1, Yi Jisuo
State block media 6 with a thickness of D1, and L1=d1-D1, and L1With D1Proportionate relationship are as follows: L1: D1=(0.05~100): 1.
Another preferred embodiment of reaction of low temperature plasma equipment of the invention is provided below in conjunction with Fig. 2
Structure, specifically:
The consersion unit has collet core structure, and the consersion unit includes:
Inner cylinder 1, reactant entrance (11) and product exit are respectively arranged on the inner cylinder (1), and the number of inner cylinder 1 is 2
More than a, the top and bottom of each inner cylinder 1, which respectively correspond, to be communicated；
Outer cylinder 2, the outer cylinder 2 are nested in the outside of each inner cylinder 1, and are respectively arranged on the outer cylinder 2 thermally conductive
Medium inlet 21 and heat-conducting medium outlet 22, can be distributed in each institute by the heat-conducting medium that the heat-conducting medium entrance 21 introduces
It states between inner cylinder 1, and the heat-conducting medium is drawn by heat-conducting medium outlet 22；
Central electrode 3, the central electrode 3 are separately positioned in each inner cylinder 1；
Grounding electrode 4, the material for forming the grounding electrode 4 is solid conductive material, and the grounding electrode 4 is formed respectively
At least partly side wall or the grounding electrode 4 of a inner cylinder 1 are circumferentially positioned at the inner sidewall of each inner cylinder 1 respectively
On；
Block media 6, in each inner cylinder 1, the block media 6 is circumferentially positioned at the central electrode 3 and institute
It states between grounding electrode 4, and is all larger than 0, Yi Jisuo with the distance between the central electrode 3 and the grounding electrode 4 respectively
The setting position for stating block media makes the region of discharge between the central electrode and the grounding electrode be situated between by the blocking
Matter interval；
Wherein, in each inner cylinder 1, the inner sidewall of the lateral wall of the central electrode 3 and the grounding electrode it
Between distance be d1 and the block media 6 with a thickness of D1, and L1=d1-D1, and L1With D1Proportionate relationship are as follows: L1: D1
=(0.05~100): 1.
In above-mentioned Fig. 1 and Fig. 2, there are also following preferred technical characteristics:
It is preferred that the consersion unit further includes ground line 5, the lateral wall of the outer cylinder 2, and one end is arranged in the ground line 5
It is connect with the grounding electrode 4.
It is preferred that the top of the inner cylinder 1 is arranged in the reactant entrance 11, the product exit is arranged in the inner cylinder 1
Lower part and/or bottom.
It is preferred that the heat-conducting medium entrance 21 and the heat-conducting medium outlet 22 be separately positioned on the outer cylinder 2 lower part and
Top.
Under preferable case, in specific embodiment shown in Fig. 1, the product exit includes 12 He of product gas outlet
Liquid product outlet 13, and the product gas outlet 12 be arranged in the inner cylinder 1 lower part and the liquid product outlet
13 are arranged in the bottom of the inner cylinder 1.
Preferably, in specific embodiment shown in Fig. 1, the product gas outlet 12 is arranged in the region of discharge
Lower section, and height H of the setting position of the product gas outlet 12 relative to 1 bottom of inner cylinder1With the region of discharge
The length L in domain2Between proportionate relationship are as follows: H1: L2=1:(0.05~25000)；Preferably H1: L2=1:(0.1~10000)；
More preferably H1: L2=1:(0.5~1000).
Under preferable case, in specific embodiment shown in Fig. 2, the product exit include product gas outlet (not
Show) and liquid product outlet (not shown), and the lower part of all inner cylinders 1 is arranged in the product gas outlet, and
The bottom of all inner cylinders 1 is arranged in the liquid product outlet.Under preferable case, the size of each inner cylinder 1 is identical.
Under preferable case, in specific embodiment shown in Fig. 2, product gas outlet setting is put described in the whole
The lower section in electric region, and height H of the setting position of the product gas outlet relative to 1 bottom of inner cylinder1It is put with described
The length L in electric region2Between proportionate relationship are as follows: H1: L2=1:(0.05~25000)；Preferably H1: L2=1:(0.1~
10000)；More preferably H1: L2=1:(0.5~1000).
Particularly, the fixed form of block media 6 is not defined in Fig. 1 and Fig. 2 of the invention, as previously mentioned,
There is no particular limitation for fixed form of the present invention to block media, and those skilled in the art should not be construed as to limit of the invention
System.
Reaction of low temperature plasma equipment provided by the invention also has the advantages that following specific:
(1) consersion unit uses conductive solids material as grounding electrode, compared with liquid grounding electrode, such ground connection
The micro discharge electric current that electric discharge generates when electrode cooperates structure of the invention is bigger, and the electric discharge for being more advantageous to hydrogen sulfide molecule is decomposed instead
It answers.
(2) setting is jacket structured on the outside of consersion unit grounding electrode, can by heat-conducting medium temperature in control collet come
Temperature control is carried out to consersion unit, hydrogen sulfide electric discharge can be made to decompose the sulphur generated and smoothly flow out region of discharge, avoid sulphur solidifying
Admittedly blocking consersion unit, make continual and steady progress of discharging.
(3) consersion unit passes through control L1(the distance between lateral wall and the inner sidewall of grounding electrode of central electrode
It is d1 and block media with a thickness of D1, and L1=d1-D1) with the thickness D of the block media1Proportionate relationship are as follows: L1:
D1=(0.05~100): 1, preferably L1: D1=(0.1~30): 1, cooperate remaining structure of consersion unit of the invention, can make
The conversion ratio for obtaining hydrogen sulfide significantly improves and decomposes energy consumption reduction.
The present invention will be described in detail by way of examples below.In following embodiment, in the feelings being not particularly illustrated
Under condition, the various raw materials used are all from commercially available.
The thickness of block media in following embodiment and comparative example is all the same.
The conversion ratio of hydrogen sulfide is calculated according to the following formula in following instance:
Molal quantity/premature cure hydrogen molal quantity × 100% of the hydrogen sulfide of the conversion ratio %=conversion of hydrogen sulfide
The energy consumption of decomposing hydrogen sulfide is detected by oscillograph and is calculated using Lissajou's figure and obtained in following instance.
Embodiment 1
Vulcanization hydroperoxide decomposition reaction, reaction of low temperature plasma are carried out using reaction of low temperature plasma equipment shown in FIG. 1
The specific structure and structural parameters of equipment are as follows:
Consersion unit includes:
Inner cylinder is respectively arranged with reactant entrance, product gas outlet and liquid product outlet on the inner cylinder, wherein
The side wall of the inner cylinder is formed by grounding electrode, and the material for forming the grounding electrode is stainless steel metal foil,
Outer cylinder, the outer cylinder is nested in the outside of the inner cylinder, and heat-conducting medium entrance is respectively arranged on the outer cylinder
It is exported with heat-conducting medium；
The axial centerline of the inner cylinder is arranged in central electrode, the central electrode, forms the central electrode
Material is stainless steel metal stick；
The lower edge of central electrode in the present embodiment is lower than the lower edge of the grounding electrode；
Block media, the material for forming the block media is hard glass；
The distance between inner sidewall of lateral wall of central electrode and grounding electrode for d1 and block media with a thickness of
D1, and L1=d1-D1, L1With the thickness D of block media1Ratio be 6:1；
Height H of the setting position of product gas outlet relative to the inner cylinder bottom1With described containing block media
The length L of region of discharge2Between proportionate relationship are as follows: H1: L2=1:46；
The volume of the consersion unit inner cylinder of the present embodiment is 0.2L.
Gaseous mixture enters in inner cylinder from the top of the inner cylinder of consersion unit in the present embodiment, and from positioned at consersion unit inner cylinder
The product gas outlet of lower part draws gaseous product, and elemental sulfur is drawn from the liquid product outlet for being located at consersion unit bottom；With
And the heat-conducting medium of the present embodiment is introduced from the lower part of the outer cylinder of consersion unit, and is drawn from the top of the outer cylinder of consersion unit.
The operating procedure of reaction of low temperature plasma equipment:
It is passed through nitrogen into the inner cylinder of reaction of low temperature plasma equipment from reactant entrance, to remove in region of discharge
Air, and gas is drawn from product gas outlet and liquid product outlet.Meanwhile it being introduced from heat-conducting medium entrance into outer cylinder
Heat-conducting medium (specially dimethicone), the heat-conducting medium of introducing is exported from heat-conducting medium draws, and the temperature of heat-conducting medium is protected
Hold is 145 DEG C.
Then H is passed through into the inner cylinder of reaction of low temperature plasma equipment from reactant entrance2S/Ar gaseous mixture, wherein H2S
Volume fraction is 20%, control gaseous mixture flow velocity make gas region of discharge mean residence time be 11.2s.H2S/Ar mixing
After gas is passed through consersion unit 30min, ac high voltage source is connected, makes central electrode and grounding electrode by adjusting voltage and frequency
Between formed plasma discharge field.Wherein discharging condition are as follows: voltage 17.2kV, frequency 8.5kHz, electric current 0.80A.
Hydrogen sulfide gas is ionized in region of discharge, is decomposed into hydrogen and elemental sulfur, the elemental sulfur for generation of discharging along inner tube wall slowly
It flows down, product liquid interval is released.Gas is flowed out from product gas outlet after reaction.
As a result: the vulcanization hydroperoxide decomposition reaction of the present embodiment measures H after persistently carrying out 20min2S conversion ratio is 74.1%；And
Continuous discharge 100h has not yet to see exception, discharge condition and H2S conversion ratio keeps stable.And the decomposition energy consumption of the present embodiment is
13.2eV/H2S molecule (1 molecule H of every decomposition2The energy that S needs is 13.2eV).
Comparative example 1
This comparative example carries out vulcanization hydroperoxide decomposition reaction, institute using reaction of low temperature plasma equipment similar to Example 1
Unlike:
Grounding electrode in this comparative example is liquid grounding electrode, and be molten condition molar ratio be 1:1 LiCl with
AlCl3, which is also heat-conducting medium, and keeping temperature is 145 DEG C, and is placed in consersion unit outer cylinder.
Control gaseous mixture flow velocity make gas region of discharge mean residence time be 18.5s.
The volume of the consersion unit inner cylinder of this comparative example is 0.05L.
Remaining is in the same manner as in Example 1.
And this comparative example carries out vulcanization hydroperoxide decomposition reaction using operating method same as Example 1.
As a result: the vulcanization hydroperoxide decomposition reaction of this comparative example measures H after persistently carrying out 20min2S conversion ratio is 15.4%, is held
H after continuous electric discharge 1.5h2S conversion ratio is reduced to 5.0%.
The decomposition energy consumption of this comparative example is 104eV/H2S molecule.
Comparative example 2
This comparative example is carried out using reaction of low temperature plasma equipment similar with comparative example 1, except that:
L in this comparative example1With the thickness D of block media1Ratio be 0.01:1.
Control gaseous mixture flow velocity make gas region of discharge mean residence time be 18.5s；
The volume of the inner cylinder of this comparative example is 0.02L.
Remaining is identical with comparative example 1.
As a result: the vulcanization hydroperoxide decomposition reaction of this comparative example measures H after persistently carrying out 20min2S conversion ratio is 20.7%, is held
H after continuous electric discharge 1.5h2S conversion ratio is reduced to 4.3%.
The decomposition energy consumption of this comparative example is 140eV/H2S molecule.
Embodiment 2
The present embodiment carries out the decomposition reaction of hydrogen sulfide using plasma reaction equipment similar to Example 1, and institute is different
, in the present embodiment:
Grounding electrode is arranged on the inner sidewall of inner cylinder, and the material for forming the grounding electrode is stainless steel metal foil；
L1With the thickness D of block media1Ratio be 20:1；
H1With the length L of the region of discharge containing block media2Between proportionate relationship are as follows: H1: L2=1:300.
H is passed through into the inner cylinder of reaction of low temperature plasma equipment from reactant entrance in the present embodiment2S/Ar gaseous mixture,
Wherein H2S volume fraction be 30%, control gaseous mixture flow velocity make gas region of discharge mean residence time be 9.6s.H2S/
After Ar gaseous mixture is passed through consersion unit 30min, ac high voltage source is connected, makes central electrode by adjusting voltage and frequency and connects
Plasma discharge field is formed between ground electrode.Wherein discharging condition are as follows: voltage 18.5kV, frequency 10.5kHz, electric current are
1.05A。
Remaining is in the same manner as in Example 1.
As a result: the vulcanization hydroperoxide decomposition reaction of the present embodiment measures H after persistently carrying out 20min2S conversion ratio is 73.4%；And
Continuous discharge 100h has not yet to see exception, discharge condition and H2S conversion ratio keeps stable.And the decomposition energy consumption of the present embodiment is
14.1eV/H2S molecule.
Embodiment 3
Vulcanization hydroperoxide decomposition reaction, reaction of low temperature plasma are carried out using reaction of low temperature plasma equipment shown in Fig. 2
The specific structure and structural parameters of equipment are as follows:
Consersion unit includes:
4 inner cylinders are respectively corresponded at the top and bottom of each inner cylinder and are communicated, and the size of 4 inner cylinders is identical, institute
The side wall for stating inner cylinder is formed by grounding electrode, and the material for forming the grounding electrode is stainless steel metal foil；
Outer cylinder, the outer cylinder is nested in the outside of the inner cylinder, and heat-conducting medium entrance is respectively arranged on the outer cylinder
It exports with heat-conducting medium, can be distributed between each inner cylinder by the heat-conducting medium that the heat-conducting medium entrance introduces, and
And the heat-conducting medium is exported by the heat-conducting medium and is drawn；
The axial centerline of each inner cylinder is arranged in central electrode, the central electrode, forms the middle electrocardio
The material of pole is stainless steel metal stick, and the central electrode in each inner cylinder is connected in parallel；
The lower edge of central electrode in the present embodiment is flushed with the lower edge of the grounding electrode.
Block media, the material for forming the block media is hard glass；
In each inner cylinder, L1With the thickness D of the block media1Ratio be 0.5:1；
H1With L2Between proportionate relationship are as follows: H1: L2=1:150；
The volume of the entire consersion unit inner cylinder of the present embodiment is 1L.
Gaseous mixture enters in inner cylinder from the top of consersion unit inner cylinder in the present embodiment, and draws gas from product gas outlet
Body product, elemental sulfur are drawn from the liquid product outlet for being located at bottom；And the heat-conducting medium of the present embodiment is from consersion unit
The lower part of outer cylinder introduces, and draws from the top of the outer cylinder of consersion unit.
The operating procedure of plasma reaction device:
It is passed through nitrogen into the inner cylinder of consersion unit from reactant entrance, to remove the air in region of discharge, and gas
Body is drawn from product gas outlet and liquid product outlet.Meanwhile heat-conducting medium (tool is introduced into outer cylinder from heat-conducting medium entrance
Body is dimethicone), the heat-conducting medium of introducing is exported from heat-conducting medium draws, and the temperature of heat-conducting medium remains 145 DEG C.
Then H is passed through into the inner cylinder of consersion unit from reactant entrance2S/Ar gaseous mixture, wherein H2S volume fraction is
65%, control gaseous mixture flow velocity make gas region of discharge mean residence time be 12.0s.H2S/Ar gaseous mixture is passed through reaction
After equipment 30min, ac high voltage source is connected, makes formation etc. between central electrode and grounding electrode by adjusting voltage and frequency
Plasma discharge field.Wherein discharging condition are as follows: voltage 15.2kV, frequency 850Hz, electric current 2.5A.Hydrogen sulfide gas exists
Region of discharge ionizes, and is decomposed into hydrogen and elemental sulfur, and the elemental sulfur for generation of discharging slowly is flowed down along inner tube wall, and from liquid
Product exit outflow.Gas is flowed out from product gas outlet after reaction.
As a result: the vulcanization hydroperoxide decomposition reaction of the present embodiment measures H after persistently carrying out 20min2S conversion ratio is 74.0%；And
Continuous discharge 100h has not yet to see exception, discharge condition and H2S conversion ratio keeps stable.And the decomposition energy consumption of the present embodiment is
14.1eV/H2S molecule.
Embodiment 4
The present embodiment carries out the decomposition reaction of hydrogen sulfide using plasma reaction equipment similar to Example 1, and institute is different
, in the present embodiment:
L1With the thickness D of block media1Ratio be 35:1.
Remaining is in the same manner as in Example 1.
As a result: the vulcanization hydroperoxide decomposition reaction of the present embodiment measures H after persistently carrying out 20min2S conversion ratio is 70.5%；And
Continuous discharge 100h has not yet to see exception, discharge condition and H2S conversion ratio keeps stable.And the decomposition energy consumption of the present embodiment is
22.8eV/H2S molecule.
Point of hydrogen sulfide is carried out using reaction of low temperature plasma equipment provided by the invention it can be seen from the above results
The conversion ratio and consersion unit provided by the invention that hydrogen sulfide can be improved when solution compared with the existing technology significantly can be
High hydrogen sulfide conversion ratio is kept to long period under low decomposition energy consumption.
The preferred embodiment of the present invention has been described above in detail, and still, the present invention is not limited thereto.In skill of the invention
In art conception range, can with various simple variants of the technical solution of the present invention are made, including each technical characteristic with it is any its
Its suitable method is combined, and it should also be regarded as the disclosure of the present invention for these simple variants and combination, is belonged to
Protection scope of the present invention.
Claims (15)
1. a kind of reaction of low temperature plasma equipment, which has with shaft jacket core structure, and the consersion unit packet
It includes:
Inner cylinder (1) is respectively arranged with reactant entrance (11) and product exit on the inner cylinder (1)；
Outer cylinder (2), the outer cylinder (2) are nested in the outside of the inner cylinder (1), and are respectively arranged on the outer cylinder (2) thermally conductive
Medium inlet (21) and heat-conducting medium outlet (22)；
Central electrode (3), the central electrode (3) are arranged in the inner cylinder (1)；
Grounding electrode (4), the material for forming the grounding electrode (4) is solid conductive material, in grounding electrode (4) formation
At least partly side wall or the grounding electrode (4) of cylinder (1) are circumferentially positioned on the inner sidewall of the inner cylinder (1)；And
Block media (6), the block media (6) be circumferentially positioned at the central electrode (3) and the grounding electrode (4) it
Between, and 0 and the block media are all larger than with the distance between the central electrode (3) and the grounding electrode (4) respectively
Setting position make the region of discharge between the central electrode and the grounding electrode by the block media interval；
Wherein, the distance between inner sidewall of lateral wall Yu the grounding electrode of the central electrode (3) is d1 and described
Block media (6) with a thickness of D1, and L1=d1-D1, and L1With D1Proportionate relationship are as follows: L1: D1=(0.05~100): 1.
2. reaction of low temperature plasma equipment according to claim 1, wherein L1: D1=(0.1~30): 1.
3. reaction of low temperature plasma equipment according to claim 1, wherein the block media (6) is fixedly connected with institute
State the top and/or bottom of inner cylinder (1)；Preferably,
One end that the inner cylinder (1) is fixedly connected in the block media (6) is provided with pore structure, so that in the inner cylinder (1)
Reactants and products can be entered or be drawn by the pore structure.
4. reaction of low temperature plasma equipment described in any one of -3 according to claim 1, wherein the inner cylinder (1)
Number is 1.
5. reaction of low temperature plasma equipment described in any one of -3 according to claim 1, wherein the inner cylinder (1)
Number be 2 or more, and be respectively arranged in each inner cylinder (1) central electrode (3), the grounding electrode (4) and
The block media (6).
6. reaction of low temperature plasma equipment according to claim 5, wherein each central electrode (3) is in parallel even
It connects；Preferably,
Each grounding electrode (4) is connected in parallel.
7. reaction of low temperature plasma equipment described in any one of -3 according to claim 1, wherein form the blocking and be situated between
The material of matter is electrically insulating material；Preferably,
Form at least one of the material of the block media in glass, quartz, ceramics, enamel, polytetrafluoroethylene (PTFE) and mica
Kind.
8. reaction of low temperature plasma equipment described in any one of -3 according to claim 1, wherein the consersion unit also wraps
It includes ground line (5), the lateral wall in the outer cylinder (2) is arranged in the ground line, and one end is connect with the grounding electrode (4).
9. reaction of low temperature plasma equipment described in any one of -3 according to claim 1, wherein the reactant entrance
(11) setting is arranged on the top of the inner cylinder (1), the product exit in the lower part and/or bottom of the inner cylinder (1).
10. reaction of low temperature plasma equipment according to claim 9, wherein the product exit includes gaseous product
(12) and liquid product outlet (13) are exported, and the product gas outlet (12) is arranged in the lower part of the inner cylinder (1), and
Bottom of liquid product outlet (13) setting in the inner cylinder (1).
11. reaction of low temperature plasma equipment according to claim 10, wherein product gas outlet (12) setting
In the lower section of the region of discharge, and the setting position of the product gas outlet (12) is relative to the inner cylinder (1) bottom
Height H1With the length L of the region of discharge2Between proportionate relationship are as follows: H1: L2=1:(0.05~25000)；Preferably H1: L2
=1:(0.1~10000)；More preferably H1: L2=1:(0.5~1000).
12. reaction of low temperature plasma equipment described in any one of -3 according to claim 1, wherein the heat-conducting medium
Entrance (21) and heat-conducting medium outlet (22) are separately positioned on the lower part and top of the outer cylinder (2).
13. reaction of low temperature plasma equipment according to claim 1, wherein form the material of the grounding electrode (4)
Selected from graphite-pipe, metal tube, metal foil or metal mesh.
14. reaction of low temperature plasma equipment according to claim 1, wherein form the material of the central electrode (3)
Selected from least one of graphite-pipe, metal bar, metal tube and graphite rod.
15. a kind of method of decomposing hydrogen sulfide, low temperature plasma of this method described in any one of claim 1-14
Implement in consersion unit, this method comprises: entering the unstripped gas containing hydrogen sulfide from reactant under the conditions of dielectric barrier discharge
Mouth is introduced to the decomposition reaction that hydrogen sulfide is carried out in the inner cylinder of the reaction of low temperature plasma equipment, the logistics obtained after decomposition
It is drawn by the product exit, also, by continuing from heat-conducting medium entrance to outside the reaction of low temperature plasma equipment
Heat-conducting medium is introduced in cylinder and the heat-conducting medium is drawn by heat-conducting medium outlet and maintains the reaction of low temperature plasma
Temperature needed for equipment, the dielectric barrier discharge are formed by grounding electrode, block media and central electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810136025.2A CN110127601A (en) | 2018-02-09 | 2018-02-09 | The method of reaction of low temperature plasma equipment and decomposing hydrogen sulfide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810136025.2A CN110127601A (en) | 2018-02-09 | 2018-02-09 | The method of reaction of low temperature plasma equipment and decomposing hydrogen sulfide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110127601A true CN110127601A (en) | 2019-08-16 |
Family
ID=67568094
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810136025.2A Pending CN110127601A (en) | 2018-02-09 | 2018-02-09 | The method of reaction of low temperature plasma equipment and decomposing hydrogen sulfide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110127601A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110935295A (en) * | 2019-12-11 | 2020-03-31 | 重庆工商大学 | Rotary concentric circle dielectric barrier micro-gap discharge pollutant treatment device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002338203A (en) * | 2001-05-22 | 2002-11-27 | National Institute Of Advanced Industrial & Technology | Method for generating hydrogen by low temperature plasma |
| US20100300872A1 (en) * | 2009-06-01 | 2010-12-02 | Chevron U.S.A. Inc. | Methods for Low Temperature Hydrogen Sulfide Dissociation |
| CN102408095A (en) * | 2011-08-20 | 2012-04-11 | 大连理工大学 | Method of decomposing hydrogen sulfide for preparation of hydrogen and elemental sulfur |
| CN103204467A (en) * | 2013-04-24 | 2013-07-17 | 滨州学院 | Device and method for continuously and steadily decomposing and making up hydrogen with hydrogen sulfide |
| CN103204466A (en) * | 2013-04-24 | 2013-07-17 | 滨州学院 | Device and method for preparing hydrogen through temperature controlled continuous decomposition of hydrogen sulfide |
| WO2014138013A1 (en) * | 2013-03-04 | 2014-09-12 | Drexel University | Plasma dissociation of hydrogen sulfide in the presence of oxygen |
-
2018
- 2018-02-09 CN CN201810136025.2A patent/CN110127601A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002338203A (en) * | 2001-05-22 | 2002-11-27 | National Institute Of Advanced Industrial & Technology | Method for generating hydrogen by low temperature plasma |
| US20100300872A1 (en) * | 2009-06-01 | 2010-12-02 | Chevron U.S.A. Inc. | Methods for Low Temperature Hydrogen Sulfide Dissociation |
| CN102408095A (en) * | 2011-08-20 | 2012-04-11 | 大连理工大学 | Method of decomposing hydrogen sulfide for preparation of hydrogen and elemental sulfur |
| WO2014138013A1 (en) * | 2013-03-04 | 2014-09-12 | Drexel University | Plasma dissociation of hydrogen sulfide in the presence of oxygen |
| CN103204467A (en) * | 2013-04-24 | 2013-07-17 | 滨州学院 | Device and method for continuously and steadily decomposing and making up hydrogen with hydrogen sulfide |
| CN103204466A (en) * | 2013-04-24 | 2013-07-17 | 滨州学院 | Device and method for preparing hydrogen through temperature controlled continuous decomposition of hydrogen sulfide |
Non-Patent Citations (1)
| Title |
|---|
| 赵冲等: "介质阻挡放电等离子体脱除硫化氢的能效优化研究" * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110935295A (en) * | 2019-12-11 | 2020-03-31 | 重庆工商大学 | Rotary concentric circle dielectric barrier micro-gap discharge pollutant treatment device |
| CN110935295B (en) * | 2019-12-11 | 2022-07-26 | 重庆工商大学 | Rotary concentric circular dielectric barrier micro-gap discharge pollutant treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11691119B2 (en) | Low temperature plasma reaction device and hydrogen sulfide decomposition method | |
| CN208553684U (en) | Reaction of low temperature plasma device | |
| CN208577431U (en) | Plasma reactor | |
| CN111278533B (en) | Plasma reaction apparatus and method for decomposing hydrogen sulfide | |
| CN208561680U (en) | High-throughput reaction of low temperature plasma device | |
| CN208553673U (en) | High-throughput plasma reaction device | |
| CN208554137U (en) | Grating type plasma reaction device | |
| CN110124482A (en) | The method of reaction of low temperature plasma device and decomposing hydrogen sulfide | |
| CN208561681U (en) | Reaction of low temperature plasma equipment | |
| CN110127601A (en) | The method of reaction of low temperature plasma equipment and decomposing hydrogen sulfide | |
| CN110124471A (en) | The method of the high-throughput low-temperature plasma system and decomposing hydrogen sulfide of decomposing hydrogen sulfide | |
| CN208561688U (en) | Grating type high throughput plasma reactor | |
| CN110127623A (en) | The method of plasma decomposing hydrogen sulfide | |
| CN110127605A (en) | The method of reaction of low temperature plasma device and decomposing hydrogen sulfide | |
| CN110127604A (en) | The method of plasma reactor and decomposing hydrogen sulfide | |
| CN110127626A (en) | The method of plasma reaction device and decomposing hydrogen sulfide | |
| CN110127603A (en) | The method of high-throughput reaction of low temperature plasma device and decomposing hydrogen sulfide | |
| CN111377409A (en) | Plasma apparatus and method for decomposing hydrogen sulfide | |
| CN110124469A (en) | The method of high-throughput plasma reaction device and decomposing hydrogen sulfide | |
| CN110124470A (en) | The method of grating type plasma reaction device and decomposing hydrogen sulfide | |
| CN110124598A (en) | The method of the low-temperature plasma device and decomposing hydrogen sulfide of decomposing hydrogen sulfide | |
| CN110127627A (en) | The method of the low-temperature plasma system and decomposing hydrogen sulfide of decomposing hydrogen sulfide | |
| CN110127624A (en) | The method of grating type high throughput plasma reactor and decomposing hydrogen sulfide | |
| CN110127621A (en) | The method of the grating type plasma system and decomposing hydrogen sulfide of decomposing hydrogen sulfide | |
| CN110124492A (en) | The processing method of H 2 S-containing gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |