CN1472838A - Nickel-cadmium cell alkali liquor producing device and producing method for alkali liquor - Google Patents
Nickel-cadmium cell alkali liquor producing device and producing method for alkali liquor Download PDFInfo
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- CN1472838A CN1472838A CNA021353352A CN02135335A CN1472838A CN 1472838 A CN1472838 A CN 1472838A CN A021353352 A CNA021353352 A CN A021353352A CN 02135335 A CN02135335 A CN 02135335A CN 1472838 A CN1472838 A CN 1472838A
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
A manufacturing device and method of Ni-Cd battery lye, among of them the manufacturing device includes No.1\2\3\4 storage tank, proportioning tank, synthesizing tank; in each storage tank and synthesizing tank sets the blender, filter screen, solenoid valve, compression pump, switch component; due to improvement to the original manufacturing technic of electrolysis lye, using the definite purpose device, overcome the memories problem of the original Ni-Cd battery electrolysis lye, extend its useful life, reduced the volume, increase the charging numbers from 400-500 to 1000; can charge or discharge at any time, shorten the charging time from 4-6 hours to 2-3 hours, take the convenience to the users.
Description
Technical field:
The invention belongs to the battery production field, particularly be nickel-cadmium cell alkali lye process units and production method thereof in the storage battery.
Background technology:
Alkali lye is by artificial directly production fluid injection in the production of nickel-cadmium cell alkali lye, people healthy there is great harm, and the battery alkali lye of producing, exist serious memory problems, seriously restricted the useful life of battery, and have long shortcoming of charging interval, a lot of units all make great efforts to address these problems in the labor intensive material resources, but do not see ripe reported in literature so far.
Summary of the invention:
The purpose of this invention is to provide a kind of technology that solves the nickel-cadmium cell memory problems preferably, and reduce the nickel-cadmium cell alkali lye process units and the production method thereof in its charging interval.
The objective of the invention is to solve like this, accompanying drawings is as follows:
A kind of nickel-cadmium cell alkali lye process units, its structure is as follows:
1. whole device is made up of housing 1, batch can 2, No. two batch cans 3, No. three batch cans 4, No. four batch cans 5, material-compound tank 6, synthetic batch cans 7; Establish blender 2-5,3-5,4-5,5-5,6-1,7-1 in each batch can respectively;
2. the upper end of 2,3,4,5 four batch cans of one, two, three, No. four batch can is respectively equipped with powder inlet pipe 2-1 and feed tube 2-3, powder inlet pipe 3-1 and feed tube 3-3, powder inlet pipe 4-1 and feed tube 4-3, powder inlet pipe 5-1 and feed tube 5-3; Wherein batch can 2,3,4 lower ends are communicated with material-compound tank 6 upper walls by pipe 2-6,3-6,4-6 respectively, and material-compound tank 6 lower walls are communicated with synthetic batch can 7 upper walls by pipe 6-4; No. four batch can 5 lower ends also are communicated with synthetic batch can 7 upper walls by pipe 5-6;
3. the drain pipe 7-6 that synthetic batch can 7 lower walls are provided with valve 7-5 stretches out housing 1 outer wall.
A kind of production method of nickel-cadmium cell alkali lye is:
Potassium hydroxide, NaOH, lithium hydroxide, in molten respectively and the water to reach saturation condition, press 10-15: 2-6: the mixed of part of 28-32 together, after the stirred for several minute, add the cadmium sulfate with the synthetic back of above-mentioned three raw materials total weight parts equal parts again, carry out getting final product after the stirred for several minute.
It is of the present invention that the good results are evident, since improved the manufacture craft of electrolytic lye in original battery,, overcome the lower-order questions in the former nickel-cadmium cell electrolyte technology, prolonged the useful life of battery, existing charging times has been reached more than 1000 times from 400-500 time; And realized can charging at any time and character such as discharge, shortened the charging interval, foreshortened to 2-3 hour with original charging 4-6 hour can finish, bring great convenience to the user, make nickel-cadmium cell alkali lye of the present invention more be adapted to demands of social development.
Description of drawings:
Accompanying drawing 1 is a nickel-cadmium cell alkali lye process units surface structure schematic diagram
Accompanying drawing 2 is a nickel-cadmium cell alkali lye process units cross-sectional view
Accompanying drawing 3 is a nickel-cadmium cell alkali lye process units circuit diagram
By accompanying drawing 1 as can be known, this device profile housing 1 is square shell, and the panel 1-1 of its upper surface goes up the material pipe that respectively carries switch for stretching: feed tube 2-1 and switch 2-2 thereof on feed pot 2, powder inlet pipe 2-3 and switch 2-4 thereof; Feed tube 3-1 and switch 3-2 thereof on No. two feed pots 3, powder inlet pipe 2-3 and switch 2-4 thereof; Feed tube 4-1 and switch 4-2 thereof on No. three feed pots 4, powder inlet pipe 4-3 and switch 44 thereof; Feed tube 5-1 and switch 5-2 thereof on No. four feed pots 5, powder inlet pipe 5-3 and switch 5-4 thereof; The front panel of housing 1 is console panel 1-2, is provided with required electronic control knob 8,9,10,11,12,13,14,15,16,17,18,19,20 in the production on console panel 1-2; At housing 1 drain pipe 7-4 and the switch 7-5 thereof that stretches out in the housing 1 arranged on side plate, the liquid outlet 7-6 of drain pipe flows out is memoryless finished product battery alkali lye.
Can find out that by accompanying drawing 2 one, two, three, No. four batch can 2,3,4,5 upper end are connected with feed tube 2-1 and powder inlet pipe 2-3, feed pipe 3-1 and powder inlet pipe 3-3, feed tube 4-1 and powder inlet pipe 4-3, feed tube 5-1 and powder inlet pipe 5-3 respectively: establish blender 2-5,3-5,4-5,5-5 respectively in one, two, three, No. four batch can 2,3,4,5 upper wall; Wherein one, two, No. three batch can 2,3,4 lower end upper wall of respectively establishing pipe 2-6,3-6, the material-compound tank 6 of 4-6 below it is communicated with; On pipe 2-6,3-6,4-6, establish filter screen 2-9,3-9,4-9 respectively successively, electromagnetically operated valve 2-7,3-7,4-7, force (forcing) pump 2-8,3-8,4-8; In material-compound tank 6 upper walls, establish blender 6-1, establish waste material mouth 6-2, establish pipe 6-6 at material-compound tank 6 lower walls and be communicated with, and on pipe 6-6, establish screen pack 6-3, switch 6-4, force (forcing) pump 6-5, switch 6-7 successively with synthetic batch can 7 upper walls at material-compound tank 6 lower walls; In synthetic batch can 7 upper walls, establish blender 7-1, establish waste material mouth 7-2 at synthetic batch can 7 lower walls; Wherein No. four batch can 5 lower ends directly are communicated with synthetic batch can 7 upper walls by pipe 5-6, establish screen pack 5-9, electromagnetically operated valve 5-7, force (forcing) pump 5-8 successively on pipe 5-6; Establish drain pipe 7-4 at synthetic batch can 7 lower walls, establish force (forcing) pump 7-3 on drain pipe 74, the liquid outlet 7-6 of the belt switch 7-5 of drain pipe 7-4 stretches out housing 1 outer wall; In battery case, add the above-mentioned electrolyte prepared, battery change into 3 fill 3 put after, just can use.
Embodiment;
In conjunction with above-mentioned battery alkali lye process units and production method thereof according to potassium hydroxide: NaOH: lithium hydroxide=13: 6: 33 i.e. each example of 13 parts, 6 parts, 33 parts is described as follows:
1. weigh up 13 parts in potassium hydroxide, 6 parts in NaOH, 33 parts of lithium hydroxides according to the above ratio, open switch 2-2,2-4, potassium hydroxide and water are entered batch can 2 No. one by pipe 2-3,2-1 respectively, starting electric switch 11 stirred blender 2-5 10-22 minute, state reaches capacity, static then 3-8 minute, stand-by;
2. weigh up 6 parts in NaOH according to the above ratio, open switch 3-2,3-4, NaOH water is entered batch can 3 No. two by tube cell, liquid pipe 3-3,3-1 respectively, starting electric switch 10 stirred blender 3-5 10-22 minute, the state that reaches capacity, static then 3-8 minute, stand-by;
3. weigh up 33 parts of lithium hydroxides according to the above ratio, open switch 4-2,4-4, lithium hydroxide and water are entered batch can 4 No. three by tube cell, liquid pipe 4-3,4-1 respectively, starting electric switch 9 stirred blender 4-5 10-22 minute, the state that reaches capacity, static then 3-8 minute, stand-by;
4. stand-by liquid stirs above-mentioned batch can 2,3,4, flow out by pipe 2-6,3-6,4-6, start electric switch 18,19 respectively, liquid is through screen pack 2-9,3-9,4-9 separately, and electromagnetically operated valve 2-7,3-7,4-7 and force (forcing) pump 2-8,3-8,4-8 flow in the material-compound tank 6, starts electric switch 12, starting blender 6-1, to carry out liquid processing synthetic, stir the 15-25 minute state that reaches capacity, static 3-8 minute, stand-by;
5. weigh up 52 parts of the cadmium sulfates of equal parts by the total weight of raw material in the material-compound tank 6, enter batch can 5 No. four by tube cell, liquid pipe 5-3, the 5-1 of the switch 5-4, the 5-2 that open respectively with ion exchange water, starting electric switch 8 stirred blender 5-5 10-22 minute, state reaches capacity, static then 3-8 minute, stand-by;
6. starting electric switch 13,14,15,16,17,18,19 simultaneously makes the liquid in the material-compound tank 6 enter synthesis tank 7 by screen pack 6-3, electromagnetic switch 6-4 and force (forcing) pump 6-5 in pipe 6-3 and the pipe, and require No. four stand-by liquid in the batch can 5 to enter in the synthesis tank 7 through filter screen 5-9, electromagnetic switch 5-7, force (forcing) pump 5-8 by pipe 5-6, synthesize processing, blender 7-1 carries out stirring in 15-25 minute, after static 3-8 minute, by drain pipe 7-4 behind force (forcing) pump 7-3, switch 7-5, flowing out through liquid outlet 7-6, promptly is finished product electrolyte.The slag liquid that residue outlet 6-2,7-2 flow out can be recycled.
The present invention does not have special processing request, and the colleague technical staff can finish.
Claims (7)
1, a kind of nickel-cadmium cell alkali lye process units is characterized in that:
1. whole device is made up of housing 1, batch can 2, No. two batch cans 3, No. three batch cans 4, No. four batch cans 5, material-compound tank 6, synthetic batch cans 7; Establish blender 2-5,3-5,4-5,5-5,6-1,7-1 in each batch can respectively:
2. the upper end of 2,3,4,5 four batch cans of one, two, three, No. four batch can is respectively equipped with powder inlet pipe 2-1 and feed tube 2-3, powder inlet pipe 3-1 and feed tube 3-3, powder inlet pipe 4-1 and feed tube 4-3, powder inlet pipe 5-1 and feed tube 5-3; Wherein batch can 2,3,4 lower ends are communicated with material-compound tank 6 upper walls by pipe 2-6,3-6,4-6 respectively, and material-compound tank 6 lower walls are communicated with synthetic batch can 7 upper walls by pipe 6-4; No. four batch can 5 lower ends also are communicated with synthetic batch can 7 upper walls by pipe 5-6;
3. synthetic batch can 7 lower walls are established the drain pipe 7-6 that has valve 7-5 and are stretched out housing 1 outer wall.
2, nickel-cadmium cell alkali lye process units according to claim 1 is characterized in that: establish switch 2-2 on feed tube 2-1, establish switch 2-4 on the powder inlet pipe 2-3; Establish switch 3-2 on the feed tube 3-1, establish switch 3-4 on the powder inlet pipe 3-3; Establish switch 4-2 on the feed tube 4-1, establish switch 4-4 on the powder inlet pipe 4-3; Establish switch 5-2 on the feed tube 5-1, establish switch 5-4 on the powder inlet pipe 5-3; Establish electronic control knob electric switch 8,9,10,11,12,13,14,15,16,17,18,19,20 on the front console panel 1-2 of housing 1, and respectively with blender 2-5,3-5,4-5,5-5,6-1,7-1, electromagnetically operated valve 2-7,3-7,4-7,5-7, force (forcing) pump 2-8,3-8,4-8,5-8 are by the corresponding connection of lead.
3, nickel-cadmium cell alkali lye process units according to claim 1, it is characterized in that: on pipe 2-6,3-6,4-6,5-6, establish screen pack 2-9,3-9,4-9,5-9 successively respectively, electromagnetically operated valve 2-7,3-7,4-7,5-7, force (forcing) pump 2-8,3-8,4-8,5-8.
4, nickel-cadmium cell alkali lye process units according to claim 1 is characterized in that: establish waste material mouth 6-2 at material-compound tank 6 lower walls; On pipe 6-6, establish screen pack 6-3, switch 6-4, force (forcing) pump 6-5, switch 6-7 successively.
5, nickel-cadmium cell alkali lye process units according to claim 1 is characterized in that: establish drain pipe 7-4 at synthetic batch can 7 lower walls, establish force (forcing) pump 7-3 on drain pipe 7-4; Establish waste material mouth 6-2,7-2 respectively at material-compound tank 6 and synthetic batch can 7 lower walls.
6, a kind of above-mentioned nickel-cadmium cell alkali lye production method, it is characterized in that: potassium hydroxide, NaOH, lithium hydroxide, soluble in water respectively to reach saturation condition, press 10-15: 2-6: the mixed of part of 28-32 together, after the stirred for several minute, add the cadmium sulfate liquid after the saturation condition that reaches with the synthetic back of above-mentioned three raw materials total weight parts equal parts again, stir and got final product in 3-15 minute.
7, nickel-cadmium cell alkali lye production method according to claim 6 is characterized in that:
1. weigh up 13 parts in potassium hydroxide, 6 parts in NaOH, 33 parts of lithium hydroxides according to the above ratio, open switch 2-2,2-4, potassium hydroxide and water are entered batch can 2 No. one by pipe 2-3,2-1 respectively, starting electric switch 11 stirred blender 2-5 10-22 minute, state reaches capacity, static then 3-8 minute, stand-by;
2. weigh up 6 parts in NaOH according to the above ratio, open switch 3-2,3-4, NaOH water is entered batch can 3 No. two by tube cell, liquid pipe 3-3,3-1 respectively, starting electric switch 10 stirred blender 3-5 10-22 minute, the state that reaches capacity, static then 3-8 minute, stand-by;
3. weigh up 33 parts of lithium hydroxides according to the above ratio, open switch 4-2,4-4, lithium hydroxide and water are entered batch can 4 No. three by tube cell, liquid pipe 4-3,4-1 respectively, starting electric switch 9 stirred blender 4-5 10-22 minute, the state that reaches capacity, static then 3-8 minute, stand-by;
4. start electric switch 18,19, with the stand-by liquid that stirs in above-mentioned one, two, No. three batch can 2,3,4, flow out by pipe 2-6,3-6,4-6 respectively, and in pipe, passing through screen pack 2-9,3-9,4-9 separately, electromagnetically operated valve 2-7,3-7,4-7 and force (forcing) pump 2-8,3-8,4-8 flow in the material-compound tank 6, start electric switch 12, starting blender 6-1, to carry out liquid processing synthetic, stir the 20-25 minute state that reaches capacity, static 3-8 minute, stand-by;
5. weigh up 52 parts of the cadmium sulfates of equal parts by the total weight of raw material in the material-compound tank 6, enter batch can 5 No. four by tube cell, liquid pipe 5-3, the 5-1 of the switch 5-4, the 5-2 that open respectively with ion exchange water, starting electric switch 8 stirred blender 5-5 10-22 minute, state reaches capacity, static then 3-8 minute, stand-by;
6. starting electric switch 13,14,15,16,17,18,19 simultaneously makes the liquid in the material-compound tank 6 enter synthesis tank 7 by screen pack 6-3, electromagnetic switch 6-4 and force (forcing) pump 6-5 in pipe 6-3 and the pipe; Simultaneously the stand-by liquid in No. four batch cans 5 is entered in the synthesis tank 7 by pipe 5-6, synthesize processing, blender 7-1 stirred 15-25 minute, after static 3-8 minute, being flowed out through liquid outlet 7-6 by switch 7-5 under force (forcing) pump 7-3 effect by drain pipe 7-4, promptly is finished product electrolyte.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA021353352A CN1472838A (en) | 2002-08-02 | 2002-08-02 | Nickel-cadmium cell alkali liquor producing device and producing method for alkali liquor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA021353352A CN1472838A (en) | 2002-08-02 | 2002-08-02 | Nickel-cadmium cell alkali liquor producing device and producing method for alkali liquor |
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| CN1472838A true CN1472838A (en) | 2004-02-04 |
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| CNA021353352A Pending CN1472838A (en) | 2002-08-02 | 2002-08-02 | Nickel-cadmium cell alkali liquor producing device and producing method for alkali liquor |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106848407A (en) * | 2017-02-27 | 2017-06-13 | 安徽桑瑞斯环保新材料有限公司 | A kind of alkaline battery electrolyte for rechargeable alkaline electrochemical cell |
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2002
- 2002-08-02 CN CNA021353352A patent/CN1472838A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106848407A (en) * | 2017-02-27 | 2017-06-13 | 安徽桑瑞斯环保新材料有限公司 | A kind of alkaline battery electrolyte for rechargeable alkaline electrochemical cell |
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