CN202181219U - Ultrasonic-electric field coupling metal aluminum primary battery reactor - Google Patents

Ultrasonic-electric field coupling metal aluminum primary battery reactor Download PDF

Info

Publication number
CN202181219U
CN202181219U CN 201120154263 CN201120154263U CN202181219U CN 202181219 U CN202181219 U CN 202181219U CN 201120154263 CN201120154263 CN 201120154263 CN 201120154263 U CN201120154263 U CN 201120154263U CN 202181219 U CN202181219 U CN 202181219U
Authority
CN
China
Prior art keywords
ultrasonic
electrode
reactor
reactor drum
aluminium
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
CN 201120154263
Other languages
Chinese (zh)
Inventor
胡劲
王玉天
文劲松
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.)
Kunming Posh Precious Metals Co Ltd
Original Assignee
Kunming Posh Precious Metals Co Ltd
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 Kunming Posh Precious Metals Co Ltd filed Critical Kunming Posh Precious Metals Co Ltd
Priority to CN 201120154263 priority Critical patent/CN202181219U/en
Application granted granted Critical
Publication of CN202181219U publication Critical patent/CN202181219U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • Y02E60/128

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The utility model discloses an ultrasonic-electric field coupling metal aluminum primary battery reactor used for preparing high-purity aluminum oxide powder. The reactor comprises an ultrasonic controller (1), a stainless-steel reactor outer layer (2), two solution bath layers (external heating) (3), an inert electrode (4), an ammeter (5), a stirrer (6), an aluminium foil electrode (7), a stainless-steel reactor inner layer (polytetrafluoroethylene inner liner) (8) and an ultrasonic transducing head (9), wherein the ultrasonic transducing head (9) is fixed or connected to the bottom of the reactor; the temperature of solution bath is 50 to 100 DEG C; the solution bath adopts to methods including external heating circulation and inner heating circulation; and the aluminum foil electrode and the inertia electrode are connected with each other through the ammeter (5) or other resistive load. Based on the fundamental principle of ultrasonic electrochemistry, the reactor constructs metal aluminum-air primary battery electrode reaction under the action of ultrasonic in a purified water system. The reactor has the advantages of simple principle, simple structure, low energy consumption, environment protection, and no environment pollution.

Description

Ultrasonic-field coupled metallic aluminium galvanic cell reactor drum
Technical field
The utility model relate to a kind of ultrasonic-field coupled metallic aluminium galvanic cell reactor drum, be used to prepare the high purity aluminium oxide powder, belong to high purity aluminium oxide powdered preparation field special device.
Background technology
The preparation method of domestic and international high purity alumina powder has multiple, but the production cycle is long, complex procedures, and the process link is many, the difficult control of purity, production cost is high, and environmental pollution is serious, and energy consumption is big.
" hydrolysis of ultrasonic activation metallic aluminium prepares Al to patent of invention 2O 3Method " (CN101332997) utilize the metallic aluminium chemically reactive higher; characteristics that can hydrolytic reactions after the aluminium of active condition is met water; utilize ultrasonic activation technology to eliminate the influence of metallic aluminium surface compact sull, promote the hydrolysis reaction of metallic aluminium effectively, successfully prepared the high purity aluminium oxide powder; this technical process is short, specific volume is little, impurity is controlled environmental friendliness easily.But reaction mechanism still is subject to the degree of metallic aluminium surface active.
Metallic aluminium has bigger electropotential and (2.7V), can constitute the galvanic cell (aluminium-air cell) that discharges efficiently with oxygen electrode as a kind of active metal.Aluminium-air cell is able to comparatively deep research as the large power supply of electromobile the eighties in eighties of last century; It has that energy density is big, light weight, pollution-free, long lifetime, high reliability and characteristics such as safe in utilization; Also exist simultaneously the problem that some can not be ignored; As very strong avidity is arranged between (1) metallic aluminium and the oxygen, in the air and the aqueous solution, the surface generates the fine and close passive oxidation film of one deck; Make the electropotential of aluminium in neutral solution not reach due theoretical electropotential, the voltage delay phenomenon when also causing discharge simultaneously.(2) aluminium is typical amphoteric metal, and activity is higher, is prone to be corroded rapidly with acid, alkali effect.(3) although current potential can reach in basic soln-14V (vs Hg/HgO), can directly as the anode material in the basic soln, but aluminium self-discharge in basic soln is bigger, produces a large amount of hydrogen, has reduced the utilization ratio of electrode, influences the battery works better.Because above problem, aluminium-air cell is difficult to use as electrical source of power always.
And from can the knowing on the other hand of things, hinder its some characteristics as battery applications and can utilize preparation high purity aluminium oxide powder just.But the sull of metallic aluminium surface compact all is a technology barrier regardless of still being for preparing the high purity aluminium oxide powder for aluminium-air cell.
Summary of the invention
The utility model purpose be to provide a kind of ultrasonic-field coupled metallic aluminium galvanic cell reactor drum, be used to prepare the high purity aluminium oxide powder.It can promote the galvanic cell reaction of aluminium-air cell to carry out effectively, also can promote the carrying out of following metallic aluminium hydrolysis reaction.
The purpose of the utility model is to accomplish like this:
Metallic aluminium galvanic cell reactor drum comprises: the outer stainless steel layer (2) of ultrasonic controller (1), reactor drum, the outer zone of heating (3) of solution bath), stainless steel layer (8) in the noble electrode (4), reometer (5), whisking appliance (6), aluminium foil electrode (7), reactor drum, inner liner polytetrafluoroethylene and ultrasonic transduction head (9); Wherein, ultrasonic transduction head (9) is fixed in reactor bottom or employing is connected in reactor bottom; Solution bath layer (3) is double-deck, and the solution bath temperature is at 50~100 ℃, with outer heating cycle and internal heating dual mode; Connect with reometer (5) or other ohmic load forms between aluminium foil electrode and the noble electrode.
The ultrasonic frequency of said ultrasonic generating unit is at 20KHZ~2000KHZ, and ultrasonic power is 10W~3000W.
Said aluminium foil electrode can be purchased on market, or adopts mode such as rolling, cutting to make, and size can be confirmed according to the reactor drum size, does not do particular requirement, and the metallic aluminium purity range is between 99~99.999%.
Said noble electrode is platinum electrode, palladium-silver electrode, ruthenium titanium electrode or platinized and titanized anode material, is shaped as sheet, net, band, silk or bundle, and the noble electrode surface-area is 1.2~5 times of aluminium foil electrode surface area.
Said reaction medium is pure water or other inorganic or organic basic solution, and the resistivity of pure water is at 1~20M Ω .cm.
This utility model equipment is based on the ultrasonic electrochemical ultimate principle; In pure aquatic system; Construct the galvanic cell electrode reaction of metallic aluminium-air down in ultrasonication; Cavatition with ultrasonic field is carried out in-situ activation to high pure metal aluminium surface, can promote the metallic aluminium surface active, and and then the galvanic cell reaction of promotion metallic aluminium-air and the hydrolysis reaction of metallic aluminium.
The utility model metallic aluminium galvanic cell reactor drum; Comprise: (1) ultrasonic controller, (2) reactor drum outer (stainless steel), (3) solution bath layer (outer heating), (4) noble electrode, (5) reometer, (6) whisking appliance, (7) aluminium foil electrode, (8) reactor drum internal layer (stainless steel, inner liner polytetrafluoroethylene) and (9) ultrasonic transduction head; Wherein, ultrasonic transduction head (9) is fixed in reactor bottom or employing is connected in reactor bottom; Solution bath layer (3) is double-deck, and the solution bath temperature is at 50~100 ℃, with outer heating cycle and internal heating dual mode; Connect with reometer (5) or other ohmic load forms between aluminium foil electrode and the noble electrode.Because in this device, under ultrasonic-field coupled condition, the hydrolysis reaction of reaction of the galvanic cell of metallic aluminium-air and metallic aluminium is gentle controlled, high-purity Al that obtains (OH) 3The gel primary particle size is little, can reach nanoscale, and even particle size distribution is active high, good fluidity.
The utility model principle of device is simple; Simple for structure, energy consumption is low, environmental friendliness, non-environmental-pollution; Be a kind ofly continue, efficient, contactless physically activated mode can make to be in state of activation in the metallic aluminium surface water solution environmental; Can promote the galvanic cell reaction of aluminium-air cell to carry out effectively, also can promote the carrying out of following metallic aluminium hydrolysis reaction.
Description of drawings
Fig. 1 is the metallic aluminium galvanic cell reactor drum of the utility model.
Among the figure; 1, ultrasonic controller, 2, reactor drum outer (then stainless steel is outer), 3, water-bath layer (; Be outer zone of heating), 4, noble electrode, 5, reometer, 6, whisking appliance, 7, aluminium foil electrode, 8, reactor drum internal layer (stainless steel, inner liner polytetrafluoroethylene), 9, ultrasonic transduction head.
Embodiment
Further specify the flesh and blood of the utility model below in conjunction with accompanying drawing with instance, but content of the present invention is not limited to this.
Like Fig. 1; The metallic aluminium galvanic cell reactor drum of the utility model; Comprise: stainless steel layer 8 in ultrasonic controller 1, the outer stainless steel layer 2 of reactor drum, the outer zone of heating 3 of solution bath, noble electrode 4, reometer 5, whisking appliance 6, aluminium foil electrode 7, the reactor drum, inner liner polytetrafluoroethylene and ultrasonic transduction head 9; Wherein, ultrasonic transduction head 9 is fixed in reactor bottom or employing is connected in reactor bottom; Solution bath layer 3 is double-deck, and the solution bath temperature is at 50~100 ℃, with outer heating cycle and internal heating dual mode; Connect with reometer 5 or other ohmic load forms between aluminium foil electrode and the noble electrode.
Wherein, ultrasonic transduction head 9 is fixed in reactor bottom or employing is connected in reactor bottom; Water-bath layer 3 is double-deck, and bath temperature is at 50~100 ℃, with outer heating cycle and internal heating dual mode; Connect with reometer 5 or other ohmic load forms between aluminium foil electrode and the noble electrode.The ultrasonic frequency of ultrasonic generating unit is at 20KHZ~2000KHZ, and ultrasonic power is 10W~3000W.The aluminium foil electrode can be purchased on market, or adopts mode such as rolling, cutting to make, and size can be confirmed according to the reactor drum size, does not do particular requirement, and the metallic aluminium purity range is between 99~99.999%.Noble electrode is platinum electrode, palladium-silver electrode, ruthenium titanium electrode or platinized and titanized anode material, is shaped as sheet, net, band, silk or bundle, and the noble electrode surface-area is 1.2~5 times of aluminium foil electrode surface area.Reaction medium is pure water or other inorganic or organic basic solution, and the resistivity of pure water is at 1~20M Ω .cm.
Embodiment 1: reactor inner container adopts liner to adopt the stainless steel preparation (thickness 0.8mm) of tetrafluoroethylene; φ 250mm; Four φ 20mm of inner bag bottom impact briquetting, the protruding column of H=10mm places the ultrasonic transduction head in it; It is 20KHZ that each ultrasonic transduction head connects ultrasonic frequency, and power is the ultra-sonic generator of 100W.Still (thickness 0.8mm, φ 300mm constitute interlayer with inner bag to outer courage, and the water of outer heating is injected in middle circulation, 50~100 ℃ of water temperature controls with the stainless steel preparation.Aluminium foil is that purity is high-purity aluminium flake of 99.999%, is of a size of: 5 * 3 * 0.1mm, noble electrode adopt the metal platinum chip size to be: 6 * 6 * 0.08mm, external whisking appliance, power 1Kw, stir speed (S.S.) 50-300 rev/min.
Embodiment 2: reactor inner container adopts liner to adopt the stainless steel preparation (thickness 0.8mm) of tetrafluoroethylene; φ 500mm; Inner bag bottom impact briquetting eight equally distributed φ 20mm, the protruding column of H=10mm places the ultrasonic transduction head in it; It is 20KHZ that each ultrasonic transduction head connects ultrasonic frequency, and power is the ultra-sonic generator of 100W.Still (thickness 0.8mm, φ 550mm constitute interlayer with inner bag to outer courage, and the middle water that injects adopts the internal heating mode, 50~100 ℃ of water temperature controls with the stainless steel preparation.Aluminium foil is that purity is high-purity aluminium flake of 99.999%, is of a size of: 10 * 6 * 0.1mm, noble electrode adopt the platinized and titanized anode net to be of a size of: 15 * 15 * 0.08mm, being fixed as one whisking appliance, power 10Kw, stir speed (S.S.) 50-300 rev/min.

Claims (4)

1. ultrasonic-field coupled metallic aluminium galvanic cell reactor drum; It is characterized in that comprising: the outer stainless steel layer (2) of ultrasonic controller (1), reactor drum, the outer zone of heating (3) of solution bath), stainless steel layer (8) in the noble electrode (4), reometer (5), whisking appliance (6), aluminium foil electrode (7), reactor drum, inner liner polytetrafluoroethylene and ultrasonic transduction head (9); Wherein, ultrasonic transduction head (9) is fixed in reactor bottom or employing is connected in reactor bottom; Solution bath layer (3) is double-deck, and the solution bath temperature is at 50~100 ℃, with outer heating cycle and internal heating dual mode; Connect with reometer (5) or other ohmic load forms between aluminium foil electrode and the noble electrode.
2. according to claim 1 ultrasonic-field coupled metallic aluminium galvanic cell reactor drum, it is characterized in that: the ultrasonic frequency of said ultrasonic generating unit is at 20KHZ~2000KHZ, and ultrasonic power is 10W~3000W.
3. according to claim 1 ultrasonic-field coupled metallic aluminium galvanic cell reactor drum; It is characterized in that: said noble electrode is platinum electrode, palladium-silver electrode, ruthenium titanium electrode or platinized and titanized anode material; Be shaped as sheet, net, band, silk or bundle, the noble electrode surface-area is 1.2~5 times of aluminium foil electrode surface area.
4. according to claim 1 ultrasonic-field coupled metallic aluminium galvanic cell reactor drum,, it is characterized in that: said reaction medium is pure water or other inorganic or organic basic solution, and the resistivity of pure water is at 1~20M Ω .cm.
CN 201120154263 2010-05-17 2011-05-14 Ultrasonic-electric field coupling metal aluminum primary battery reactor Expired - Fee Related CN202181219U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201120154263 CN202181219U (en) 2010-05-17 2011-05-14 Ultrasonic-electric field coupling metal aluminum primary battery reactor

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN201020192110.X 2010-05-17
CN201020192110 2010-05-17
CN 201120154263 CN202181219U (en) 2010-05-17 2011-05-14 Ultrasonic-electric field coupling metal aluminum primary battery reactor

Publications (1)

Publication Number Publication Date
CN202181219U true CN202181219U (en) 2012-04-04

Family

ID=46174265

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201120154263 Expired - Fee Related CN202181219U (en) 2010-05-17 2011-05-14 Ultrasonic-electric field coupling metal aluminum primary battery reactor

Country Status (1)

Country Link
CN (1) CN202181219U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104303360A (en) * 2012-05-04 2015-01-21 Ifp新能源公司 System comprising accumulators and air-aluminium batteries
CN106596390A (en) * 2017-02-16 2017-04-26 天津大学 Electrochemical reaction kettle with double liners and application method thereof
CN109980322A (en) * 2019-04-22 2019-07-05 南京航空航天大学 Ultrasonic wave added type metal-air battery working method and system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104303360A (en) * 2012-05-04 2015-01-21 Ifp新能源公司 System comprising accumulators and air-aluminium batteries
CN106596390A (en) * 2017-02-16 2017-04-26 天津大学 Electrochemical reaction kettle with double liners and application method thereof
CN106596390B (en) * 2017-02-16 2023-08-11 天津大学 Electrochemical reaction kettle with double inner containers and application method thereof
CN109980322A (en) * 2019-04-22 2019-07-05 南京航空航天大学 Ultrasonic wave added type metal-air battery working method and system
CN109980322B (en) * 2019-04-22 2021-04-13 南京航空航天大学 Ultrasonic-assisted metal-air battery working method and system

Similar Documents

Publication Publication Date Title
CN104993159B (en) A kind of bifunctional catalyst and its preparation and the application in metal-air battery
CN105591080B (en) A kind of lithium ion battery negative material SiOX-TiO2The preparation method of/C
CN107017450B (en) Aluminium-air cell
CN103915613B (en) Hydrothermal reaction coupling spray pyrolysis MnO2The preparation method of/Graphene electrodes material
CN103972496B (en) A kind of hydrothermal reaction coupling spray pyrolysis prepares Co3O4The method of/graphene nano combination electrode material
CN102324505A (en) Preparation method of graphene loaded with anatase type nano titanium dioxide and application thereof
CN106129344A (en) A kind of tin ash/Titanium dioxide spherical granule and the preparation method of graphene nano belt composite
CN202181219U (en) Ultrasonic-electric field coupling metal aluminum primary battery reactor
CN103474636B (en) Silica-based lithium ion battery cathode material and its preparation method
CN103820807A (en) Device and method for producing hydrogen and generating electricity
CN103700868B (en) The preparation method of a kind of magnadure air cell and Catalytic Layer thereof
CN102820136A (en) High-energy-density supercapacitor
CN106602087A (en) Nickel-cobalt-manganese-carbon nanotube difunctional composite catalyst and preparation method and application thereof
CN106935807A (en) A kind of ammonium vanadate/nickel foam sodium-ion battery preparation method of self-supporting positive pole
CN104993127B (en) A kind of preparation method of titanium-oxide-coated anode material for lithium-ion batteries
CN103606656B (en) A kind of preparation method of the lead oxide/graphene nanocomposite material for plumbous charcoal superbattery
CN103887528B (en) Lithium-air battery MnO2-RuO2/ C catalyst and preparation method thereof
CN108383106A (en) A kind of preparation method of graphene/activated carbon microballon
CN105609791A (en) La-Co-Mn and carbon nanotube dual-functional composite catalyst and preparation and application thereof
CN108091822B (en) Preparation method of positive electrode of magnesium cuprous chloride battery and battery obtained by preparation method
CN106449181B (en) A kind of preparation method of polypyrrole/graphene/tin dioxide composite material
CN103531854A (en) Novel power supply with comprehensive performances of supercapacitor and zinc-silver battery
CN103578784B (en) Nanometer copper oxide composite material and preparation method thereof and super-capacitor electrode and super-capacitor
CN106299318A (en) silicon-based lithium ion battery cathode material and preparation method thereof
CN110165199A (en) A kind of positive electrode of modification and preparation method thereof

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120404

Termination date: 20190514

CF01 Termination of patent right due to non-payment of annual fee