CN107706434A - Chemical heater packaging and liquid flow pipe butt joint device and assembling method - Google Patents
Chemical heater packaging and liquid flow pipe butt joint device and assembling method Download PDFInfo
- Publication number
- CN107706434A CN107706434A CN201710564467.2A CN201710564467A CN107706434A CN 107706434 A CN107706434 A CN 107706434A CN 201710564467 A CN201710564467 A CN 201710564467A CN 107706434 A CN107706434 A CN 107706434A
- Authority
- CN
- China
- Prior art keywords
- chemical
- heater
- chemical heater
- heaters
- liquid
- 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.)
- Granted
Links
- 239000000126 substance Substances 0.000 title claims abstract description 132
- 239000007788 liquid Substances 0.000 title claims abstract description 78
- 238000000034 method Methods 0.000 title claims abstract description 10
- 210000001503 joint Anatomy 0.000 title abstract 2
- 238000004806 packaging method and process Methods 0.000 title abstract 2
- HTQOEHYNHFXMJJ-UHFFFAOYSA-N oxosilver zinc Chemical compound [Zn].[Ag]=O HTQOEHYNHFXMJJ-UHFFFAOYSA-N 0.000 claims description 20
- 238000005538 encapsulation Methods 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 11
- 238000003032 molecular docking Methods 0.000 claims description 11
- 229910001923 silver oxide Inorganic materials 0.000 claims description 2
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Substances [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 claims description 2
- BSWGGJHLVUUXTL-UHFFFAOYSA-N silver zinc Chemical compound [Zn].[Ag] BSWGGJHLVUUXTL-UHFFFAOYSA-N 0.000 abstract description 7
- 230000006835 compression Effects 0.000 abstract description 2
- 238000007906 compression Methods 0.000 abstract description 2
- 239000003792 electrolyte Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003721 gunpowder Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/30—Deferred-action cells
- H01M6/36—Deferred-action cells containing electrolyte and made operational by physical means, e.g. thermal cells
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Hybrid Cells (AREA)
Abstract
The invention discloses a chemical heater packaging and liquid flow pipe butt joint device and an assembling method, which are characterized in that: the chemical heater package and liquid flow tube interfacing apparatus at least comprises: two chemical heaters arranged in parallel; the two chemical heaters are positioned in the same horizontal plane; the two chemical heaters are respectively a chemical heater A and a chemical heater B; the liquid outlet of the chemical heater A and the liquid inlet of the chemical heater B are positioned on the same side; a second connecting pipe is arranged between the liquid outlet of the chemical heater A and the liquid inlet of the chemical heater B; two ends of the second connecting pipe are communicated with the two chemical heaters through compression screws; the liquid reservoirs are positioned above the two chemical heaters, and the bottoms of the liquid reservoirs are communicated with the liquid inlet of the chemical heater A through a first connecting pipe; a zinc-silver battery located below the two chemical heaters; and the liquid outlet of the chemical heater B is communicated with the liquid inlet of the zinc-silver battery through a third connecting pipe.
Description
Technical field
The present invention relates to reserve cell and battery technology field, more particularly to a kind of encapsulation of chemical heater and liquid stream
Pipe docking facilities and assemble method.
Background technology
Due to zinc-silver reserve battery have it is higher than energy, specific power is big, can heavy-current discharge, discharging voltage balance, voltage
The features such as precision is high, and reliability, security are good, is widely used in each field.
Chemical heat zinc-silver reserve battery is typically by battery-pack exterior casing, electric connector, gas generator, liquid reservoir, combination
The parts such as pole plate group, chemical heater form.Wherein, it is entirely isolated between the both positive and negative polarity inside zinc-silver reserve battery.Electricity
The activated current that external direct current power supply provides battery prescribed level is connected by electric connector when pond group uses, while by gas
Electric igniter in generator and chemical heater is lighted, and the electric igniter in gas generator and chemical heater is distinguished immediately
Heating medicine in gunpowder and chemical heater in pilot gas generator, the high pressure gas that powder burning discharges in gas generator
Body enters liquid reservoir through gas-guide pipeline, and by the electrolyte push-in activation pipeline in liquid reservoir, and it is fast that medicine is heated in chemical heater
Quick burning, which burns, discharges substantial amounts of heat, raises heat exchanger temperature, electrolyte is when flowing through chemical heater, with chemical heater
Carry out heat exchange, temperature rise.Heated electrolyte enters in composite polar plate group, makes pole plate, the barrier film in composite polar plate group
Also accordingly rise Deng parts temperature.Internal temperature of battery is increased in the preference temperature section of battery work, and battery can work
Make.Chemical heater design is the important component of chemical heat zinc-silver reserve battery.Chemical heater is by heat exchanger, heating
The parts such as device shell, chemical heat piece, the piece that ignites, ignition circuit, heat-insulation layer, heater housing are formed, and are cylindrical structure, empty
Between utilization rate it is relatively low.
Currently known chemical heater encapsulation and fluid flow tube docking facilities and method are carried out using socket-welding fitting
Connection, but the size of adapter therein and nut is larger (more than 40mm), and zinc-silver oxide cell, chemical heater and liquid reservoir etc.
Part is to be horizontally mounted.
The content of the invention
The technical problem to be solved in the present invention is:A kind of chemical heater encapsulation and fluid flow tube docking facilities and assembling are provided
Method, excessive electro-hydraulic residual when the patent can avoid horizontal positioned, and shorten length of pipe.
The present invention is adopted the technical scheme that to solve technical problem present in known technology:
A kind of chemical heater encapsulation and fluid flow tube docking facilities, are comprised at least:
Two chemical heaters (2) be arrangeding in parallel;Two chemical heaters (2) are located in the same horizontal plane;Two changes
It is respectively chemical heater A and chemical heater B to learn heater (2);The liquid outlet and chemical heater of the chemical heater A
B inlet is located at the same side;Is provided between the liquid outlet of the chemical heater A and chemical heater B inlet
Two connecting tubes (4);The both ends of second connecting tube (4) are connected by housing screw (6) with two chemical heaters;
Liquid reservoir (7) above two chemical heaters, the bottom of the liquid reservoir (7) pass through the first connecting tube
(3) inlet with chemical heater A connects;
Zinc-silver oxide cell (1) below two chemical heaters;The liquid outlet of the chemical heater B connects by the 3rd
Adapter (5) connects with the inlet of zinc-silver oxide cell (1).
A kind of chemical heater encapsulation and the assemble method of fluid flow tube docking facilities, comprise the following steps:
Step 101, parts are chosen, specific parts include:Zinc-silver oxide cell (1), two chemical heaters (2),
One connection liquid pipe (3), the second connection liquid pipe (4), the 3rd connection liquid pipe (5), liquid reservoir (7), two housing screws (6);
Step 102, above-mentioned parts are assembled, be specially:
Two chemical heaters are placed in parallel, two chemical heaters are located in the same horizontal plane;Two chemical heats
Device is respectively chemical heater A and chemical heater B;Chemical heater A liquid outlet and chemical heater B inlet are located at
The same side;One end of second connecting tube (4) is connected by a housing screw (6) with chemical heater A liquid outlet, institute
The other end for stating the second connecting tube (4) is connected by another housing screw (6) with chemical heater B inlet;
Liquid reservoir (7) is placed in the surface of two chemical heaters (2), liquid pipe (3) is connected by liquid reservoir using first
(7) inlet with chemical heater A connects;
Zinc-silver oxide cell (1) is placed in the underface of two chemical heaters (2), liquid pipe (5) is connected by chemistry using the 3rd
Heater B liquid outlet connects with the inlet of zinc-silver oxide cell (1).
The present invention has the advantages and positive effects of:
1st, the present invention can effectively reduce the chi shared by connector in chemical heater encapsulation and fluid flow tube docking facilities
Very little (below 20mm).The technical scheme of this patent can also be applied to other reserve cell systems for needing chemical heat, without office
It is limited to zinc-silver reserve battery;
2nd, the connection liquid pipe in the present invention takes full advantage of the space of chemical heater, reduces the sky shared by fluid flow tube
Between;
3rd, the present invention can realize being disposed vertically for liquid reservoir and zinc-silver oxide cell, excessive electro-hydraulic residual when avoiding horizontal positioned
Stay, and shorten the length of pipe of half.
Brief description of the drawings:
Fig. 1 is the front view of the preferred embodiment of the present invention;
Fig. 2 is the left view of the preferred embodiment of the present invention;
Fig. 3 is the front view of chemical heater in the preferred embodiment of the present invention;
Fig. 4 is the left view of chemical heater in the preferred embodiment of the present invention;
Fig. 5 is the front view of the second connection liquid pipe in the preferred embodiment of the present invention;
Fig. 6 is the shaft section figure of connector in the preferred embodiment of the present invention;
Fig. 7 is the top view of connector in the preferred embodiment of the present invention;
Fig. 8 is the front view of fluid-through tube in the preferred embodiment of the present invention.
Wherein:1st, zinc-silver oxide cell;2nd, chemical heater;3rd, the first connection liquid pipe;4th, the second connection liquid pipe;4-1, logical liquid
Pipe;4-2, connector;5th, the 3rd connection liquid pipe;6th, housing screw;7th, liquid reservoir.
Embodiment
In order to further understand the content, features and effects of the present invention, hereby enumerating following examples, and coordinate accompanying drawing
Describe in detail as follows:
Fig. 1 to Fig. 8, a kind of chemical heater encapsulation and fluid flow tube docking facilities are referred to, including:
Two chemical heaters 2 be arrangeding in parallel;Two chemical heaters 2 are located in the same horizontal plane;Two chemistry add
Hot device 2 is respectively chemical heater A and chemical heater B;The liquid outlet of the chemical heater A and entering for chemical heater B
Liquid mouth is located at the same side;The second connection is provided between the liquid outlet of the chemical heater A and chemical heater B inlet
Pipe 4;The both ends of second connecting tube 4 are connected by housing screw 6 with two chemical heaters;
Liquid reservoir 7 above two chemical heaters, the bottom of the liquid reservoir 7 pass through the first connecting tube 3 and change
Learn heater A inlet connection;
Zinc-silver oxide cell 1 below two chemical heaters;The liquid outlet of the chemical heater B passes through the 3rd connection
Pipe 5 connects with the inlet of zinc-silver oxide cell 1.
In above preferred embodiment:Second connecting tube 4 includes a fluid-through tube 4-1 and two connector 4-2;Institute
It is T-shaped threeway valve arrangement to state connector;The connector includes the transverse pipe and and chemical heat being connected with fluid-through tube
The longitudinal pipe that device 2 connects;The longitudinal pipe includes two interfaces being located along the same line;One interface of the longitudinal pipe with
Chemical heater 2 connects;The screw rod of the housing screw 6 is provided with the hollow cavity that liquid passes through, and the end of the hollow cavity is opened
Provided with the opening connected with chemical heater 2, the side wall of the hollow cavity offers the opening connected with fluid-through tube;The compression
Connector is connected by the screw rod of screw 6 after another interface insertion of longitudinal pipe with chemical heater 2;The longitudinal pipe it is interior
Footpath matches connection with the external diameter of screw rod.The fluid-through tube 4-1 is " 7 " character form structure.
A kind of chemical heater encapsulation and the assemble method of fluid flow tube docking facilities, comprise the following steps:
Step 101, parts are chosen, specific parts include:1, two chemical heater 2, first of zinc-silver oxide cell connects
Adapter 3, second connects liquid pipe the 4, the 3rd and connects 7, two liquid pipe 5, liquid reservoir housing screws 6;
Step 102, above-mentioned parts are assembled, be specially:
Two chemical heaters are placed in parallel, two chemical heaters are located in the same horizontal plane;Two chemical heats
Device is respectively chemical heater A and chemical heater B;Chemical heater A liquid outlet and chemical heater B inlet are located at
The same side;One end of second connecting tube 4 is connected by a housing screw 6 with chemical heater A liquid outlet, and described
The other end of two connecting tubes 4 is connected by another housing screw 6 with chemical heater B inlet;
Liquid reservoir 7 is placed in the surface of two chemical heaters 2, liquid pipe 3 is connected by liquid reservoir 7 and chemistry using first
Heater A inlet connection;
Zinc-silver oxide cell 1 is placed in the underface of two chemical heaters 2, liquid pipe 5 is connected by chemical heater B using the 3rd
Liquid outlet connected with the inlet of zinc-silver oxide cell 1.
The present invention operation principle be:
Zinc-silver oxide cell using when electrolyte the first connection liquid pipe 3, chemical heater A, second are passed sequentially through from liquid reservoir
Zinc-silver oxide cell is injected after connection liquid pipe 4, chemical heater B, the 3rd connection liquid pipe 5.Wherein electrolyte is flowing through chemical heater
After carry out heating and raise the temperature to design temperature.
This patent encapsulates the chi at position using zinc-silver oxide cell chemical heater after this patent compared with routine techniques
It is very little to reduce below 20mm;Being disposed vertically for liquid reservoir and zinc-silver oxide cell can be realized, it is excessive electro-hydraulic when avoiding horizontal positioned
Residual, and shorten the length of pipe of half.
Embodiments of the invention are described in detail above, but the content is only presently preferred embodiments of the present invention,
It is not to be regarded as the practical range for limiting the present invention.Any changes and modifications in accordance with the scope of the present application,
All should still it belong within the patent covering scope of the present invention.
Claims (2)
1. a kind of chemical heater encapsulation and fluid flow tube docking facilities, it is characterised in that:Comprise at least:
Two chemical heaters (2) be arrangeding in parallel;Two chemical heaters (2) are located in the same horizontal plane;Two chemistry add
Hot device (2) is respectively chemical heater A and chemical heater B;The liquid outlet of the chemical heater A and chemical heater B's
Inlet is located at the same side;The second company is provided between the liquid outlet of the chemical heater A and chemical heater B inlet
Take over (4);The both ends of second connecting tube (4) are connected by housing screw (6) with two chemical heaters;
Liquid reservoir (7) above two chemical heaters, the bottom of the liquid reservoir (7) by the first connecting tube (3) with
Chemical heater A inlet connection;
Zinc-silver oxide cell (1) below two chemical heaters;The liquid outlet of the chemical heater B passes through the 3rd connecting tube
(5) inlet with zinc-silver oxide cell (1) connects.
2. a kind of chemical heater encapsulation and the assemble method of fluid flow tube docking facilities, it is characterised in that:Comprise the following steps:
Step 101, parts are chosen, specific parts include:Zinc-silver oxide cell (1), two chemical heaters (2), first connect
Adapter (3), the second connection liquid pipe (4), the 3rd connection liquid pipe (5), liquid reservoir (7), two housing screws (6);
Step 102, above-mentioned parts are assembled, be specially:
Two chemical heaters are placed in parallel, two chemical heaters are located in the same horizontal plane;Two chemical heaters point
Wei not chemical heater A and chemical heater B;Chemical heater A liquid outlet and chemical heater B inlet are positioned at same
Side;One end of second connecting tube (4) is connected by a housing screw (6) with chemical heater A liquid outlet, and described
The other end of two connecting tubes (4) is connected by another housing screw (6) with chemical heater B inlet;
Liquid reservoir (7) is placed in the surface of two chemical heaters (2), using first connection liquid pipe (3) by liquid reservoir (7) with
Chemical heater A inlet connection;
Zinc-silver oxide cell (1) is placed in the underface of two chemical heaters (2), liquid pipe (5) is connected by chemical heat using the 3rd
Device B liquid outlet connects with the inlet of zinc-silver oxide cell (1).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710564467.2A CN107706434B (en) | 2017-07-12 | 2017-07-12 | Chemical heater packaging and liquid flow pipe butt joint device and assembling method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710564467.2A CN107706434B (en) | 2017-07-12 | 2017-07-12 | Chemical heater packaging and liquid flow pipe butt joint device and assembling method |
Publications (2)
Publication Number | Publication Date |
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CN107706434A true CN107706434A (en) | 2018-02-16 |
CN107706434B CN107706434B (en) | 2019-10-01 |
Family
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Application Number | Title | Priority Date | Filing Date |
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CN201710564467.2A Active CN107706434B (en) | 2017-07-12 | 2017-07-12 | Chemical heater packaging and liquid flow pipe butt joint device and assembling method |
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CN (1) | CN107706434B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108827680A (en) * | 2018-06-15 | 2018-11-16 | 中国电子科技集团公司第十八研究所 | Device and method for testing performance of chemical heater |
CN110504460A (en) * | 2019-07-31 | 2019-11-26 | 中国电子科技集团公司第十八研究所 | Chemical heating system and method for zinc-silver reserve battery |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202940294U (en) * | 2012-11-26 | 2013-05-15 | 梅岭化工厂 | Tangential liquid-outflow liquid reservoir of chemical heat activated zinc-silver reserve battery pack |
CN204271145U (en) * | 2014-12-10 | 2015-04-15 | 中国电子科技集团公司第十八研究所 | High-energy-density zinc-silver reserve battery electrolyte heater |
CN206116517U (en) * | 2016-10-09 | 2017-04-19 | 贵州梅岭电源有限公司 | Zinc -silver reserve cell group uses cistern |
-
2017
- 2017-07-12 CN CN201710564467.2A patent/CN107706434B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202940294U (en) * | 2012-11-26 | 2013-05-15 | 梅岭化工厂 | Tangential liquid-outflow liquid reservoir of chemical heat activated zinc-silver reserve battery pack |
CN204271145U (en) * | 2014-12-10 | 2015-04-15 | 中国电子科技集团公司第十八研究所 | High-energy-density zinc-silver reserve battery electrolyte heater |
CN206116517U (en) * | 2016-10-09 | 2017-04-19 | 贵州梅岭电源有限公司 | Zinc -silver reserve cell group uses cistern |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108827680A (en) * | 2018-06-15 | 2018-11-16 | 中国电子科技集团公司第十八研究所 | Device and method for testing performance of chemical heater |
CN110504460A (en) * | 2019-07-31 | 2019-11-26 | 中国电子科技集团公司第十八研究所 | Chemical heating system and method for zinc-silver reserve battery |
Also Published As
Publication number | Publication date |
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CN107706434B (en) | 2019-10-01 |
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