[go: up one dir, main page]

CN101671004B - Three-cavity series plasma vehicular hydrogen-rich gas generator - Google Patents

Three-cavity series plasma vehicular hydrogen-rich gas generator Download PDF

Info

Publication number
CN101671004B
CN101671004B CN2009100937297A CN200910093729A CN101671004B CN 101671004 B CN101671004 B CN 101671004B CN 2009100937297 A CN2009100937297 A CN 2009100937297A CN 200910093729 A CN200910093729 A CN 200910093729A CN 101671004 B CN101671004 B CN 101671004B
Authority
CN
China
Prior art keywords
plasma
hydrogen
rich gas
reaction
generation
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.)
Expired - Fee Related
Application number
CN2009100937297A
Other languages
Chinese (zh)
Other versions
CN101671004A (en
Inventor
李兴虎
马奎峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beihang University
Original Assignee
Beihang University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beihang University filed Critical Beihang University
Priority to CN2009100937297A priority Critical patent/CN101671004B/en
Publication of CN101671004A publication Critical patent/CN101671004A/en
Application granted granted Critical
Publication of CN101671004B publication Critical patent/CN101671004B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Hydrogen, Water And Hydrids (AREA)

Abstract

本发明提出了一种高效、快捷、轻便的三腔串联式等离子体车载富氢气体发生器,该装置外观为圆筒形,用于随车富氢气体的快速制取。该发生器主要包括等离子体反应部分和等离子体发生部分。等离子体发生部分由三个均布的发生腔串联组成,发生腔横截面的形状为120°扇形,发生腔的半径为6-8mm。反应部分即反应腔,形状为圆柱形。本装置以安装在扇形角圆心的电极为正极,以底座的弧形侧壁为负极,车载蓄电池为电源,经放电控制装置在正负电极间放电产生等离子体。当碳氢燃料或碳氢燃料与空气的混合物由底部进气口进入发生腔,经过火花放电使反应物产生等离子体。之后,反应物进入反应腔进行部分氧化反应,迅速变为富氢气体,并由上方的出口排出。

Figure 200910093729

The present invention proposes an efficient, fast and portable three-cavity serial plasma vehicle-mounted hydrogen-rich gas generator. The device has a cylindrical appearance and is used for rapid production of vehicle-mounted hydrogen-rich gas. The generator mainly includes a plasma reaction part and a plasma generation part. The plasma generation part is composed of three evenly distributed generation chambers in series, the shape of the cross section of the generation chamber is 120° sector, and the radius of the generation chamber is 6-8mm. The reaction part is the reaction chamber, which is cylindrical in shape. The device uses the electrode installed in the center of the fan-shaped corner as the positive pole, the arc-shaped side wall of the base as the negative pole, and the on-board battery as the power supply. The discharge control device discharges between the positive and negative electrodes to generate plasma. When the hydrocarbon fuel or the mixture of hydrocarbon fuel and air enters the generating chamber from the bottom air inlet, the reactant generates plasma through spark discharge. Afterwards, the reactant enters the reaction chamber for partial oxidation reaction, quickly becomes hydrogen-rich gas, and is discharged from the upper outlet.

Figure 200910093729

Description

Three-cavity series plasma vehicular hydrogen-rich gas generator
Technical field
Patent of the present invention belongs to new energy field, the effect of this device be make hydrocarbon fuel at normal temperatures and pressures apace with air generation partial oxidation reaction, produce hydrogen-rich gas rapidly.For engine provides hydrogen-rich fuel, improve flame propagation velocity, improve combustion in IC engine; Also can be used as the reducing gas of automobile catalytic cleaner, improve reduction efficiency, reduce the NO discharging; After the hydrogen-rich gas that produces is through further the purification, also can be used as the hydrogen manufacturing equipment of fuel cell car or fuel cell.
Background technology
Energy dilemma and environmental pollution have become serious day by day global problem.The petroleum resources of automobile consumption are more and more, and its expellant gas pollutent, particulate pollutant etc. have also become the principal element of urban air pollution.Therefore, improve internal-combustion engines vehicle energy conversion efficiency, reduce its noxious emission and exploitation cleaning, cheap New-type fuel and become the urgent task of automotive industry.
The combustion of hydrogen product is a water, and unique noxious emission is NOx, thereby is considered to the ideal automotive fuel.Because pure hydrogen preparation cost height, and there are the factors such as storage, transportation and safety of hydrogen jar, so be difficult to obtain large-scale practical application at present.And utilize the traditional fuel that carries with car to adopt scheme to overcome the above problems with car hydrogen manufacturing, therefore, vehicle-mounted hydrogen production is considered to one of best selection.At present, the method for vehicle-mounted hydrogen production mainly contains two kinds of traditional chemical reforming process and reforming plasma methods.
(1) chemical reforming process
Chemistry reformation ratio juris is under the effect of catalyzer, makes hydrocarbon fuel generation chemical transformation produce hydrogen, and can be divided into 3 kinds according to the difference of reformation part heat-supplying mode: external-heat steam reforming, partial oxidation are reformed, self-heating recapitalization.It is higher that the external-heat vapor reforming hydrogen production produces the hydrogen rate, but reaction process needs outside heat supply, and temperature of reaction is higher, thus system complicated, start slowly, difference in response and thermo-efficiency is low.The partial oxidation reformation hydrogen production is the technology of comparative maturity, and its product hydrogen rate is lower than the steam reforming, but because this reaction is thermopositive reaction, so do not need extra heat supply, system is simple relatively and thermo-efficiency is higher, and start time while is short, dynamic response is very fast.Self-heating recapitalization is steam reforming and partial oxidation to be reformed combine, the response of this reformation mode very fast and produce the hydrogen rate and capacity usage ratio higher, but, make hydrogen produce hydrogen rate and transformation efficiency reduction because the local superheating phenomenon appears in the imbalance of heat absorption and heat release easily.
(2) reforming plasma method
Plasma method hydrogen manufacturing be a kind ofly develop, continuous perfect novel method, the problem that it can solve or avoid the traditional chemical catforming to run into.Hydrogen manufacturing chemical principle with plasma exciatiaon roughly is identical with traditional principle, and different is to excite Activity of Chemical Reaction material difference.The active substance of traditional method is a catalyzer, and the active substance of plasma method is high-energy electron and free radical.Because what reforming plasma used is electricity, so reaction has controllability highly, can be on a large scale adjustments of gas speed and composition, reach the optimization of reaction.By means of highly active particle image electronics, ion, excited state material, the plasma physical efficiency improves chemical reaction velocity greatly, perhaps for thermo-negative reaction provides the energy, and avoids using heterogeneous catalyst.These advantages with and high-energy-density and reaction times of causing thus reduce, for hydrogen-manufacturing reactor minification, weight reduction provide may.Plasma-converted hydrogen manufacturing is not high to ingredient requirement in addition, so long as hydrogenous material, can become the raw material of plasma method hydrogen manufacturing as Sweet natural gas, alcohols, biofuel etc.
Summary of the invention
The objective of the invention is: proposed a kind of three-cavity series plasma vehicular hydrogen-rich gas generator, be used for the producing fast of car hydrogen-rich gas, the solution that reduces energy source of car consumption and hazardous emission and Hydrogen Sources of Fuel Cell Vehicles is provided is with reference to approach.
Technical scheme of the present invention is: this producer comprises that mainly part (2) takes place for plasma reaction part (1) and plasma body.Plasma reaction part (1) is a plasm reaction cavity, and this partial shape is cylindrical, and inside is partly isolated reaction chamber and generation cavity by insulation gland (4); Part (2) takes place in plasma body, and this part is composed in series by three uniform generation cavities that metab (6), insulation gland (4) and ceramic urceolus (5) form, the generation cavity cross section be shaped as 120 ° fan-shaped, the radius of generation cavity is 6-8mm.Inlet mouth (7) is positioned at the bottom, makes progress vertically, and reactant enters top reaction chamber through three fan-shaped generation cavities of series connection, is flowed out by air outlet, top (11) at last.This device is a positive pole with the electrode (3) that is installed in the fan angle center of circle, is negative pole with the curved wall (15) of base, and Vehicular accumulator cell is a power supply, discharges between positive and negative electrode through discharge control (12) device.When hydrocarbon fuel or hydrocarbon fuel and AIR MIXTURES enter generation cavity, make reactant produce plasma body through spark discharge.Afterwards, reactant enters reaction chamber (1) and carries out partial oxidation reaction, becomes hydrogen-rich gas rapidly.What reforming process was used is electricity, and reaction has the controllability of height, can be on a large scale adjustments of gas speed and composition, reach the optimization of reaction.
Advantage of the present invention is: adopt the placed in-line structure in three chambeies, utilize the reforming plasma method that hydrocarbon fuel is carried out reformation hydrogen production, advantage such as that this reactor has is efficient, rapid, light, easy realization.
Description of drawings
Fig. 1 is the vehicular hydrogen-rich gas generator exploded view.
Fig. 2 is the application synoptic diagram of vehicular hydrogen-rich gas generator.
The number in the figure explanation
The 1-reactive moieties; Part takes place in 2-; The 3-positive pole; The 4-gland that insulate; 5-pottery urceolus; The 6-reactor base; The 7-inlet mouth; The anodal open holes of 8-; The 9-platen; 10-reactor end cap; The 11-air outlet; The 12-control unit that discharges; The 13-refining plant; 14-hydrogen-rich gas using appts; 15-negative pole (bonding)
Embodiment
The structure of this vehicle-mounted hydrogen production device as shown in Figure 1.Hydrocarbon fuel or hydrocarbon fuel and AIR MIXTURES enter generation cavity 2 from inlet mouth 7, make reactant produce plasma body through spark discharge.Afterwards, reactant enters reaction chamber 1 and carries out sufficient oxidizing reaction, obtains hydrogen-rich gas rapidly.Reacted hydrogen-rich gas is discharged by air outlet 11.Adopt three placed in-line structures of generation cavity, the duration of contact of gas and electric arc and contact probability are increased, and reaction is more abundant, can obtain the hydrogen-rich gas of higher hydrogen content.
Can be designed to on-board hydrogen generation system as shown in Figure 2 in actual applications.By the isoionic generation of discharge control device 12 controls, enter cleaner 13 through ionization and abundant reacted hydrogen-rich gas, enter hydrogen-rich gas using appts 14 after the processing.Can several producers in parallel according to the actual flow needs.
This generating means has been used for the reforming plasma hydrogen manufacturing test of dimethyl ether, and the volumn concentration of hydrogen reaches 30% in the hydrogen-rich gas that obtains, and the hydrogen productive rate reaches 40%. This device can be used for the reforming plasma hydrogen-rich gas preparation of multiple hydrocarbon fuel (liquid fuels such as the gasoline after natural gas, oil liquefied gas and the vaporization and diesel oil). Experiment results shows, the advantage such as that this device has is efficient, rapid, light, easy realization.

Claims (1)

1.一种三腔串联式等离子体车载富氢气体发生器,包括:等离子体反应部分(1)即等离子体反应腔,该部分形状为圆柱形,内部由绝缘压盖(4)将反应腔与发生腔部分隔离;1. A three-cavity series plasma vehicle-mounted hydrogen-rich gas generator, comprising: a plasma reaction part (1) is a plasma reaction chamber, the part is cylindrical in shape, and the reaction chamber is enclosed by an insulating gland (4) inside. Partially isolated from the generating cavity; 等离子体发生部分(2),该部分由金属底座(6)、绝缘压盖(4)和陶瓷外筒(5)形成的三个均布的发生腔串联而成,单个发生腔横截面的形状为120°扇形,扇形半径的调整范围为6-8mm,以安装在扇形角圆心的电极(3)为正极,以底座的弧形侧壁(15)为负极,进气口(7)位于底部,沿轴向向上,经过三个串联扇形发生腔进入上面的反应腔,最后由上部出气口(11)流出。The plasma generation part (2), which is composed of three evenly distributed generation chambers formed by the metal base (6), insulating gland (4) and ceramic outer cylinder (5) in series, the shape of the cross-section of a single generation chamber It is 120° fan-shaped, and the adjustment range of the fan-shaped radius is 6-8mm. The electrode (3) installed at the center of the fan-shaped corner is used as the positive pole, and the arc-shaped side wall (15) of the base is used as the negative pole. The air inlet (7) is located at the bottom , go upward in the axial direction, pass through three series fan-shaped generating chambers and enter the upper reaction chamber, and finally flow out from the upper gas outlet (11).
CN2009100937297A 2009-10-15 2009-10-15 Three-cavity series plasma vehicular hydrogen-rich gas generator Expired - Fee Related CN101671004B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009100937297A CN101671004B (en) 2009-10-15 2009-10-15 Three-cavity series plasma vehicular hydrogen-rich gas generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009100937297A CN101671004B (en) 2009-10-15 2009-10-15 Three-cavity series plasma vehicular hydrogen-rich gas generator

Publications (2)

Publication Number Publication Date
CN101671004A CN101671004A (en) 2010-03-17
CN101671004B true CN101671004B (en) 2011-04-06

Family

ID=42018465

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009100937297A Expired - Fee Related CN101671004B (en) 2009-10-15 2009-10-15 Three-cavity series plasma vehicular hydrogen-rich gas generator

Country Status (1)

Country Link
CN (1) CN101671004B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102802334A (en) * 2012-07-31 2012-11-28 北京航空航天大学 Sliding-arc-discharge plasma generation device loaded with magnetic field
CN114768714A (en) * 2022-04-01 2022-07-22 安徽华东光电技术研究所有限公司 Non-thermal arc plasma liquid fuel gasification device and method for improving gasification efficiency

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7037484B1 (en) * 2002-06-21 2006-05-02 University Of Central Florida Research Foundation, Inc. Plasma reactor for cracking ammonia and hydrogen-rich gases to hydrogen
CN101024488A (en) * 2007-01-11 2007-08-29 武汉理工大学 Method for preparing hydogen-riched mixed gas by water-contained alcohol and its plasma recombiner
US20080314734A1 (en) * 2007-06-21 2008-12-25 The Regents Of The University Of California Carbonaceous solid fuel gasifier utilizing dielectric barrier non-thermal plasma

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7037484B1 (en) * 2002-06-21 2006-05-02 University Of Central Florida Research Foundation, Inc. Plasma reactor for cracking ammonia and hydrogen-rich gases to hydrogen
CN101024488A (en) * 2007-01-11 2007-08-29 武汉理工大学 Method for preparing hydogen-riched mixed gas by water-contained alcohol and its plasma recombiner
US20080314734A1 (en) * 2007-06-21 2008-12-25 The Regents Of The University Of California Carbonaceous solid fuel gasifier utilizing dielectric barrier non-thermal plasma

Also Published As

Publication number Publication date
CN101671004A (en) 2010-03-17

Similar Documents

Publication Publication Date Title
JP6977082B2 (en) Ammonia decomposition equipment and system and hydrogen production method
CN100364881C (en) A methanol catalytic reforming hydrogen production device using waste heat of an internal combustion engine and its control method
EP1739057A2 (en) Hydrogen fuel supply system
CN101832168B (en) Dielectric Barrier Discharge Coupled Catalyst Monolithic Reactor for NOx Removal from Diesel Engines
CN103708418B (en) Residual heat of tail gas of automobile is utilized to carry out the device of preparing hydrogen by reforming methanol
CN102431434B (en) Hydrogen cell mixed power automobile
US20070274905A1 (en) Thermal disassociation of water
CN207572466U (en) vehicle-mounted fuel cell power generation system
JP2007009917A5 (en)
CN104157889A (en) Methanol steam reforming hydrogen production reactor for fuel cell car
CN216638920U (en) Hydrogen production device
CN102802334A (en) Sliding-arc-discharge plasma generation device loaded with magnetic field
WO1998042807A1 (en) Method of production of low pollution fuel and production apparatus therefor
CN101671004B (en) Three-cavity series plasma vehicular hydrogen-rich gas generator
CN201165470Y (en) An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device
CN102020243A (en) Method for decomposing water into hydrogen-oxygen mixed gas fuel
Huang et al. Improvement in hydrogen production with plasma reformer system
CN101293634A (en) Compact type following hydrogen production plant
KR102626114B1 (en) Internal combustion engine for saving fuel and reducing exhaust gas emissions
CN202389189U (en) Hydrogen-powered hybrid car
CN100343163C (en) Spontaneous recombination system for the conversion and separation of hydrogen from aqueous methanol particles
CN107188120A (en) Utilize the hydrogen producing apparatus of catalyst chamber
CN205933210U (en) Methanol reforming reactor
CN109179321B (en) Online methanol reformer utilizing engine tail gas by adopting baffling separation mechanism
CN211111044U (en) Hydrogen production device by using automobile waste heat

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110406

Termination date: 20111015