CN109200929A - A kind of storage battery production processing acid solution device for formulating - Google Patents
A kind of storage battery production processing acid solution device for formulating Download PDFInfo
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- CN109200929A CN109200929A CN201811090387.9A CN201811090387A CN109200929A CN 109200929 A CN109200929 A CN 109200929A CN 201811090387 A CN201811090387 A CN 201811090387A CN 109200929 A CN109200929 A CN 109200929A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/813—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles mixing simultaneously in two or more mixing receptacles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/2132—Concentration, pH, pOH, p(ION) or oxygen-demand
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
- B01F35/833—Flow control by valves, e.g. opening intermittently
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/48—Mixing water in water-taps with other ingredients, e.g. air, detergents or disinfectants
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
The present invention relates to storage battery production apparatus field, specially a kind of storage battery production processing acid solution device for formulating.Technical solution is: including concentrated sulfuric acid tank, water tank, reactor tank, collecting tank, the first acid storage tank, cooling trough, circulating pump, control cabinet, multiple mixing tubes are provided in reactor tank, top is provided with concentrated sulfuric acid spray head, water spray head in mixing tube, and bottom is provided with dilute sulfuric acid conflux disk in reactor tank, top is provided with concentrated sulfuric acid conflux disk, water conflux disk；Concentrated sulfuric acid tank liquid outlet is sequentially connected concentrated sulfuric acid metering pump, concentrated sulfuric acid conflux disk, water tank liquid outlet is sequentially connected water metering pump, water conflux disk, dilute sulfuric acid conflux disk is connected with collecting tank inlet, collecting tank leakage fluid dram is connected with the first acid storage tank, cooling trough water inlet is connected with reactor tank bottom end, and cooling trough leakage fluid dram is sequentially connected circulating pump, reactor tank upper end；Concentrated sulfuric acid metering pump, water metering pump are connect with control cabinet.Production efficiency is improved, the concentration consistency of dilute sulfuric acid is good, accuracy is high.
Description
Technical field
The present invention relates to storage battery production apparatus field, specially a kind of storage battery production processing acid solution device for formulating.
Background technique
Lead-acid accumulator is made of electrode mainly by lead and its oxide, and electrolyte is a kind of battery of sulfuric acid solution.
Lead-acid accumulator has more than 100 years history from after invention so far, because it is easily obtained with cheap, raw material, makes
With there is sufficient reliability, suitable for the advantages that heavy-current discharge and extensive ambient temperature range electrochmical power source always
It has overwhelming superiority, the backup power source or main power source as equipment are widely used.Wherein electrolyte dilution heat of sulfuric acid
Preparation be its production and processing in essential process.
The dilution heat of sulfuric acid of storage battery production processing is by distilled water or deionized water diluted concentration be 98% and
Above concentrated sulfuric acid obtains, and when the concentrated sulfuric acid and water contact, a large amount of heat can be generated, acid mist and dilute sulfuric acid is caused to splash, is influenced
Environment also threatens the health of operator.Existing storage battery production is prepared dilute sulfuric acid and is mostly prepared by agitating device, although energy
The enough formation for preventing acid mist to a certain extent, but the dilute sulfuric acid temperature after stirring is excessively high, mostly at 80 DEG C or more, cannot be
With using, the production cycle is influenced.Meanwhile the concentration of dilute sulfuric acid needed for the battery of different purposes is different, therefore to being matched
The dilute sulfuric acid concentration of system is more demanding；In existing some automatic preparing devices, using metering valve, liquid level sensor or weighing
The mode of device metering does not have come the ratio for calculating the concentrated sulfuric acid and water although the dilute sulfuric acid of respective concentration can be obtained
There is detection to feed back；It is lost as caused by metering device measurement error and reaction, causes prepared dilute sulfuric acid concentration difference larger,
It cannot be guaranteed that the quality of battery.
Summary of the invention
The object of the present invention is to provide a kind of a kind of storage battery production processing acid solutions in labour-saving quick for installation, easy to adjust
Device for formulating.
For achieving the above object, the technical scheme adopted by the invention is that: acid solution is used in a kind of processing of storage battery production
Device for formulating, including concentrated sulfuric acid tank, water tank, reactor tank, collecting tank, the first acid storage tank, cooling trough, circulating pump, control cabinet,
Multiple mixing tubes are evenly provided in the reactor tank vertically, top is provided with concentrated sulfuric acid spray head, water in the mixing tube
Spray head, bottom is provided with dilute sulfuric acid conflux disk, top is provided with concentrated sulfuric acid conflux disk, water conflux disk, institute in the reactor tank
Concentrated sulfuric acid conflux disk is stated to be connected with concentrated sulfuric acid spray head, the water conflux disk is connected with water spray head, the mixing tube lower end with
Dilute sulfuric acid conflux disk is connected；The concentrated sulfuric acid tank liquid outlet is sequentially connected concentrated sulfuric acid metering pump, shut-off valve A, concentrated sulfuric acid conflux disk,
The water tank liquid outlet is sequentially connected water metering pump, shut-off valve B, water conflux disk, the dilute sulfuric acid conflux disk and collecting tank into
Liquid mouth is connected, and the collecting tank leakage fluid dram is connected with the first acid storage tank, is provided between the collecting tank and the first acid storage tank defeated
Pump is sent, the cooling trough water inlet is connected with reactor tank bottom end, and the cooling trough leakage fluid dram is sequentially connected circulating pump, reaction
Tank upper end；First acid storage tank bottom is provided with shut-off valve F, the circulating pump, concentrated sulfuric acid metering pump, water metering pump, conveying
Pump, shut-off valve A, shut-off valve B, shut-off valve F, respectively with control cabinet be electrically connected.
It preferably, further include thermostatic water bath, the collecting tank is placed in thermostatic water bath, is provided with temperature in the collecting tank
Sensor is spent, shutoff valve C, the thermostatic water bath, temperature sensor, shutoff valve C are provided between the collecting tank and delivery pump
It is electrically connected respectively with control cabinet.
Preferably, it is provided with adjustment tank between the shutoff valve C and delivery pump, is arranged between adjustment tank and the delivery pump
There is shut-off valve E, the adjustment tank top is provided with sulfuric acid concentration on-line detector, bottom is provided with agitating device, the adjustment
Tank top is connected by shut-off valve D and adjustment pump with water tank, and the shut-off valve D, shut-off valve E, adjustment pump, sulfuric acid concentration are online
Detector, the second agitating device are electrically connected with control cabinet respectively.
Preferably, the dilute sulfuric acid conflux disk upper and lower surface is provided with corresponding continuous concaveconvex structure.
Preferably, the collection pot bottom is provided with the first agitating device.
Preferably, shut-off valve G, the conveying pump output terminal are connected between the conveying pump output terminal and the first acid storage tank
Also it is connected with shut-off valve H, the second acid storage tank in turn, second acid storage tank bottom is provided with shut-off valve K, the shut-off valve G, cuts
Only valve H, shut-off valve K are electrically connected with control cabinet respectively.
Preferably, first acid storage tank, be provided with liquid level sensor in the second acid storage tank, first acid storage tank,
Liquid level sensor in second acid storage tank is electrically connected with control cabinet respectively.
The invention has the following advantages: can accurately input the required concentrated sulfuric acid and water by metering pump；?
The multiple mixing tubes of setting in reactor tank, and recycled the cooling water in cooling trough and reactor tank by circulating pump, to take away
The heat generated in mixing tube；The concentrated sulfuric acid and water are pumped into spray head by metering pump and form tiny drop in mixing tube, i.e.,
The concentrated sulfuric acid and water can be made adequately to mix, prevented also from fluid spills, dilution also can be rapidly cooled down and obtain dilute sulfuric acid；Collecting tank
The dilute sulfuric acid of generation can be sufficiently stirred again, collecting tank, which is placed in thermostatic water bath, to cool down dilute sulfuric acid again,
Adjustment tank is inputted again after so that the dilute sulfuric acid temperature exported is reached requirement by temperature sensor.
In addition, online concentration monitor is arranged in adjustment tank top, can real-time monitoring prepare resulting dilute sulfuric acid concentration, and can
Control adjustment is pumped into clear water, finely tunes the concentration of dilute sulfuric acid, it is ensured that the prepared compound preparation requirement of dilute sulfuric acid.It can also be by data
Control cabinet is fed back to, that further finely tunes the concentrated sulfuric acid and clear water is pumped into ratio, from the concentration of source control dilute sulfuric acid.Setting two
Acid storage tank, acid storage tank is interior to be arranged liquid level sensor, again accesses device for formulating in production system after an acid storage tank storage is full,
Corresponding shut-off valve is controlled by control cabinet, it is ensured that the supply of dilute sulfuric acid guarantees the contiguity of production, improves production efficiency.
Therefore the present invention, which can be realized, uses matching for dilute sulfuric acid, shortens the preparation time of dilute sulfuric acid, guarantees the company of production
Continuous property, improves the production efficiency of battery, reduces production cost, guarantees consistency and accuracy that dilute sulfuric acid is prepared.
Detailed description of the invention
Fig. 1 is the device of the invention connection schematic diagram；
Fig. 2 is the component connection schematic diagram in reactor tank of the invention；
Fig. 3 is the cross-sectional view of dilute sulfuric acid conflux disk of the invention.
Specific embodiment
In conjunction with Fig. 1-3, the detailed description present invention.
A kind of storage battery production processing acid solution device for formulating, including concentrated sulfuric acid tank 1, water tank 2, reactor tank 3, collecting tank
4, the first acid storage tank 7, cooling trough 8, circulating pump 9, control cabinet 10 are evenly provided in the reactor tank 3 multiple mixed vertically
Pipe 34 is closed, top is provided with concentrated sulfuric acid spray head 35, water spray head 36 in the mixing tube 34, and bottom is set in the reactor tank 3
Be equipped with dilute sulfuric acid conflux disk 33, top is provided with concentrated sulfuric acid conflux disk 31, water conflux disk 32, the concentrated sulfuric acid conflux disk 31 with it is dense
Sulfuric acid spray head 35 is connected, and the water conflux disk 32 is connected with water spray head 36, and 34 lower end of mixing tube and dilute sulfuric acid converge
Disk 33 is connected；1 liquid outlet of concentrated sulfuric acid tank is sequentially connected concentrated sulfuric acid metering pump 91, shut-off valve A11, concentrated sulfuric acid conflux disk 31,
2 liquid outlet of water tank is sequentially connected water metering pump 92, shut-off valve B12, water conflux disk 32.Specifically, the concentrated sulfuric acid passes through
Concentrated sulfuric acid metering pump 91 flows through concentrated sulfuric acid conflux disk 31 and forms tiny drop in mixing tube 34 by concentrated sulfuric acid spray head 35,
It is atomization in mixing tube 34 by concentrated water spray head 36 that clear water by water metering pump 92 flows through water flow row 32, therefore can make dense sulphur
Acid and clear water adequately mix, while keeping the heat generated more dispersed.Dilute sulfuric acid after dilution is received through dilute sulfuric acid conflux disk 33
Collection.
The dilute sulfuric acid conflux disk 31 is connected with 4 inlet of collecting tank, 4 leakage fluid dram of collecting tank and the first acid storage tank 7
It is connected, delivery pump 94,8 water inlet of cooling trough and reactor tank 3 is provided between the collecting tank 4 and the first acid storage tank 7
Bottom end is connected, and 8 leakage fluid dram of cooling trough is sequentially connected circulating pump 9,3 upper end of reactor tank；First acid storage tank, 7 bottom is set
It is equipped with shut-off valve F16, the circulating pump 9, concentrated sulfuric acid metering pump 91, water metering pump 92, delivery pump 94, shut-off valve A11, shut-off valve
B12, shut-off valve F16, respectively with control cabinet 10 be electrically connected.That is, circulating pump 9 will be in cooling trough and reactor tank 3
Cooling water is recycled, and the heat that diluting concentrated sulfuric acid generates in mixing tube 34 can be quickly and effectively taken away.Conflux disk 33 is collected
Dilute sulfuric acid collected by collecting tank 4, the dilute sulfuric acid that then defeated pump 94 will be collected into is pumped into the first acid storage tank 7, completes dilute sulphur
The preparation of acid.Main logic control unit is PLC in control cabinet 10, facilitates the write-in of control program, circulating pump 9, concentrated sulfuric acid meter
Amount pump 91, water metering pump 92, delivery pump 94, shut-off valve A11, shut-off valve B12, shut-off valve F16 are concentrated by control cabinet 10
Control.
It further, further include thermostatic water bath 5, the collecting tank 4 is placed in thermostatic water bath 5, is set in the collecting tank 4
It is equipped with temperature sensor, shutoff valve C 13 is provided between the collecting tank 4 and delivery pump 94, the thermostatic water bath 5, temperature pass
Sensor, shutoff valve C 13 are electrically connected with control cabinet 10 respectively.It should be understood that thermostatic water bath 5 can be further to preparation institute
The dilute sulfuric acid obtained is cooled down, and temperature sensor detects the problem of preparing resulting dilute sulfuric acid in real time, passes through control cabinet 10
Shutoff valve C 13 is controlled, only when the temperature of dilute sulfuric acid is down to required temperature, just opens shutoff valve C 13 and delivery pump 94, it will
Prepared dilute sulfuric acid is pumped into the first acid storage tank 7.
Further, adjustment tank 6, the adjustment tank 6 and delivery pump are provided between the shutoff valve C 13 and delivery pump 94
It is provided with shut-off valve E15 between 94, is provided with sulfuric acid concentration on-line detector 61 at the top of the adjustment tank 6, bottom is provided with
Two agitating devices 62 are connected at the top of the adjustment tank 6 with water tank 2 by shut-off valve D14, adjustment pump 93, the shut-off valve
D14, shut-off valve E15, adjustment pump 93, sulfuric acid concentration on-line detector 61, the second agitating device 62 are electrical with control cabinet 10 respectively
Connection.Specifically, the on-line detector 61 at adjustment tank 6 top calculates sulfuric acid by refractive index of the light in sulfuric acid solution
Concentration, therefore can in real time, accurately measure the concentration of sulfuric acid.
It is taken when the dilute sulfuric acid concentration in adjustment tank 6 meets, feeds back to control cabinet 10 and open shut-off valve E15, make dilute sulphur
Acid is pumped into the first acid storage tank 7.It is taken when the dilute sulfuric acid concentration in adjustment tank 6 is higher than, control cabinet 10 closes shut-off valve
E15, shutoff valve C 13 open shut-off valve D14, adjustment pump 93 and the second agitating device 62, to separate the defeated of front end dilute sulfuric acid
Enter, being stirred while clear water is added is uniformly mixed it, until the concentration of dilute sulfuric acid meets requirement, is then shut off
Shut-off valve D14, adjustment pump 93 and the second agitating device 62 are opened, opens shut-off valve E15, shutoff valve C 13 continues dilute sulfuric acid
It prepares；The amount of the concentrated sulfuric acid is reduced needed for calculating simultaneously by control cabinet 10, so that controlling concentrated sulfuric acid metering pump 91 reduces the concentrated sulfuric acid
Addition.It should be noted that the amount very little for the clear water being added in adjustment tank 6, therefore the heat generated when dilution is seldom,
It can be absorbed by water base of addition, therefore be not required to cool down again.It is taken, is closed when the dilute sulfuric acid concentration in adjustment tank 6 is lower than
Shut-off valve E15 is closed, while feeding back to control cabinet 10, control water metering pump 92 reduces the input of clear water, until the concentration of dilute sulfuric acid
Reach requirement, opening stop valve E15 continues the pumping of dilute sulfuric acid.It should be noted that only when concentrated sulfuric acid concentration,
When concentrated sulfuric acid metering pump, clear water metering pump inaccuracy, it just will appear above-mentioned adjustment process, and when above process adjustment process continues
Between it is very of short duration, therefore will not influence the lasting preparation of dilute sulfuric acid.
Further, 31 upper and lower surface of dilute sulfuric acid conflux disk is provided with corresponding continuous concaveconvex structure.Dilute sulfuric acid
31 upper and lower surface of conflux disk is provided with corresponding continuous concaveconvex structure, makes it have certain storage capacity；It on the one hand can be with
Certain buffer function is played, so that dilute sulfuric acid mixing is more uniform；Another side increases dilute sulfuric acid conflux disk 31 and reactor tank 3
The contact area of interior cooling water further cools down the resulting dilute sulfuric acid of preparation, to reduce the cooling of thermostatic water bath 5
Work, thus the confecting efficiency saved electric energy, improve dilute sulfuric acid.
Further, 4 bottom of collecting tank is provided with the first agitating device 41.It is understood that in collecting tank 4
The first agitating device 41 is arranged in bottom, can stir dilute sulfuric acid stored in collecting tank 4, further to ensure to be prepared
Dilute sulfuric acid even concentration, therefore can guarantee adjust 6 top of tank sulfuric acid concentration on-line detector 61 measured by dilute sulfuric acid
The accuracy of concentration.
Further, shut-off valve G17, the conveying are connected between 94 output end of delivery pump and the first acid storage tank 7
It pumps 94 output ends and is also connected with shut-off valve H18, the second acid storage tank 71 in turn, 71 bottom of the second acid storage tank is provided with shut-off valve
K19, the shut-off valve G17, shut-off valve H18, shut-off valve K19 are electrically connected with control cabinet 10 respectively.Specifically, shut-off valve
Whether G17 control dilute sulfuric acid is pumped into the first acid storage tank 7；94 output end of delivery pump is also connected with the second acid storage tank 71, shut-off valve H18
Whether control dilute sulfuric acid is pumped into the second acid storage tank 71, and shut-off valve K19 controls the production whether the second acid storage tank 71 accesses battery
System of processing.Second acid storage tank 71 can be used as the use of slack storage tank, can also be directly accessed and come into operation；It is embodied in, when
When first acid storage tank 7 is filled, continue the dilute sulfuric acid that acid solution device for formulating is prepared as slack tank, when dilute in the first acid storage tank 7
When sulfuric acid is finished, as the sour device of storage for the use of storage battery production.
Further, first acid storage tank 7, liquid level sensor, first storage are provided in the second acid storage tank 71
Liquid level sensor in sour tank 7, the second acid storage tank 71 is electrically connected with control cabinet 10 respectively.That is, control cabinet 10 passes through
Obtain the data of the first acid storage tank 7, liquid level sensor in the second acid storage tank 71, thus control shut-off valve F16, shut-off valve G17,
The opening and closing of shut-off valve H18, shut-off valve K19 realize that the first acid storage tank 7, the second acid storage tank 71 circulation access in production system.In addition
Production stops using acid it is possible that other problems, whole when the first acid storage tank 7, the second acid storage tank 71 are more than the storage upper limit
A device can be automatically stopped complex acid production,, also can portion in anti-locking apparatus prevented also from the leakage of acid solution while energy saving
Part overload, so that the component in protective device, guarantees safety in production.
Specific control flow of the invention is as follows:
By calculating the PLC amount of the required concentrated sulfuric acid and clear water being written in control cabinet 10, while by required dilute sulfuric acid
Concentration, temperature write-in control cabinet 10 in PLC in, all electric elements pass through control cabinet 10 and are controlled.
1, all shut-off valve is closed, circulating pump 9 is opened, recycles the cooling water in reactor tank 3 and cooling bath 8,
Open thermostatic water bath 5.
2, successively opening stop valve B12, water metering pump 92, shut-off valve A11, concentrated sulfuric acid metering pump 91, start to dilute dense sulphur
Acid.
3, temperature sensor detects the temperature of dilute sulfuric acid in collecting tank 4, when it is down to setting value, opening stop valve C13,
Dilute sulfuric acid is sent into adjustment tank 6.
4, the concentrated sulfuric acid concentration more obtained of sulfuric acid concentration detector 61, is adjusted, if reaching if concentration is not up to standard
Then opening stop valve E15, shut-off valve G17 and delivery pump 94 are marked, is pumped into the first acid storage tank 7 or the second acid storage tank 71.
5, when the liquid level of the first acid storage tank 7 reaches the storage upper limit, which is accessed in storage battery production acid adding system,
Circulation is carried out using the first acid storage tank 7 and the second acid storage tank 71, and dilute sulfuric acid is provided.
6, it when the liquid level in stopping production or the first acid storage tank 7, the second acid storage tank 71 arrives the upper limit, first closes all
Shut-off valve turn off other electrical equipments.
Claims (7)
1. a kind of storage battery production processing acid solution device for formulating, including concentrated sulfuric acid tank (1), water tank (2), reactor tank (3), receipts
Collect tank (4), the first acid storage tank (7), cooling trough (8), circulating pump (9), control cabinet (10), it is characterised in that:
It is evenly provided with vertically multiple mixing tubes (34) in the reactor tank (3), the interior top of the mixing tube (34) is provided with
Concentrated sulfuric acid spray head (35), water spray head (36), the interior bottom of the reactor tank (3) are provided with dilute sulfuric acid conflux disk (33), top
It is provided with concentrated sulfuric acid conflux disk (31), water conflux disk (32), the concentrated sulfuric acid conflux disk (31) and concentrated sulfuric acid spray head (35) phase
Even, the water conflux disk (32) is connected with water spray head (36), mixing tube (34) lower end and dilute sulfuric acid conflux disk (33) phase
Even；
Concentrated sulfuric acid tank (1) liquid outlet is sequentially connected concentrated sulfuric acid metering pump (91), shut-off valve A (11), concentrated sulfuric acid conflux disk
(31), water tank (2) liquid outlet is sequentially connected water metering pump (92), shut-off valve B (12), water conflux disk (32), described dilute
Sulfuric acid conflux disk (31) is connected with collecting tank (4) inlet, and collecting tank (4) leakage fluid dram is connected with the first acid storage tank (7), institute
It states and is provided between collecting tank (4) and the first acid storage tank (7) delivery pump (94), cooling trough (8) water inlet and reactor tank
(3) bottom end is connected, and cooling trough (8) leakage fluid dram is sequentially connected circulating pump (9), reactor tank (3) upper end；
First acid storage tank (7) bottom is provided with shut-off valve F (16), the circulating pump (9), concentrated sulfuric acid metering pump (91), water
Metering pump (92), delivery pump (94), shut-off valve A (11), shut-off valve B (12), shut-off valve F (16), respectively with control cabinet (10) electricity
Property connection.
2. storage battery production processing acid solution device for formulating according to claim 1, it is characterised in that: further include thermostatted water
Slot (5), the collecting tank (4) are placed in thermostatic water bath (5), are provided with temperature sensor, the receipts in the collecting tank (4)
It is provided with shutoff valve C (13) between collection tank (4) and delivery pump (94), the thermostatic water bath (5), temperature sensor, shutoff valve C
(13) it is electrically connected respectively with control cabinet (10).
3. storage battery production processing acid solution device for formulating according to claim 2, it is characterised in that: the shutoff valve C
(13) it is provided with adjustment tank (6) between delivery pump (94), is provided with cut-off between institute's adjustment tank (6) and delivery pump (94)
Valve E (15), adjustment tank (6) top is provided with sulfuric acid concentration on-line detector (61), bottom is provided with the second agitating device
(62), it is connected by shut-off valve D (14), adjustment pump (93) with water tank (2) at the top of the adjustment tank (6), the shut-off valve D
(14), shut-off valve E (15), adjustment pump (93), sulfuric acid concentration on-line detector (61), the second agitating device (62) respectively with control
Cabinet (10) is electrically connected.
4. storage battery production processing acid solution device for formulating according to claim 3, it is characterised in that: the dilute sulfuric acid converges
Flow table (31) upper and lower surface is provided with corresponding continuous concaveconvex structure.
5. storage battery production processing acid solution device for formulating according to any one of claims 1-4, it is characterised in that: institute
It states collecting tank (4) bottom and is provided with the first agitating device (41).
6. storage battery production processing acid solution device for formulating according to claim 5, it is characterised in that: the delivery pump
(94) it is connected between output end and the first acid storage tank (7) shut-off valve G (17), delivery pump (94) output end is also sequentially connected
There are shut-off valve H (18), the second acid storage tank (71), the second acid storage tank (71) bottom is provided with shut-off valve K (19), the cut-off
Valve G (17), shut-off valve H (18), shut-off valve K (19) are electrically connected with control cabinet (10) respectively.
7. storage battery production processing acid solution device for formulating according to claim 6, it is characterised in that: the first storage acid
Liquid level sensor is provided in tank (7), the second acid storage tank (71), in first acid storage tank (7), the second acid storage tank (71)
Liquid level sensor is electrically connected with control cabinet (10) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811090387.9A CN109200929A (en) | 2018-09-18 | 2018-09-18 | A kind of storage battery production processing acid solution device for formulating |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811090387.9A CN109200929A (en) | 2018-09-18 | 2018-09-18 | A kind of storage battery production processing acid solution device for formulating |
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| CN109200929A true CN109200929A (en) | 2019-01-15 |
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| CN201811090387.9A Pending CN109200929A (en) | 2018-09-18 | 2018-09-18 | A kind of storage battery production processing acid solution device for formulating |
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| CN103521123A (en) * | 2013-10-11 | 2014-01-22 | 长兴埃克森科技有限公司 | Automatic preparation system for dilute sulfuric acid |
| CN205095694U (en) * | 2015-10-16 | 2016-03-23 | 重庆华强生态肥业有限公司 | Hierarchical diluting device of concentrated sulfuric acid |
| CN205731094U (en) * | 2016-06-21 | 2016-11-30 | 佛山市安齿生物科技有限公司 | A kind of configuration system for the mixing of high concentration strong acid |
-
2018
- 2018-09-18 CN CN201811090387.9A patent/CN109200929A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020009401A1 (en) * | 1992-05-20 | 2002-01-24 | Texas Encore, Llc | Mixer and process for use |
| JP2007175691A (en) * | 2005-12-02 | 2007-07-12 | Asahi Organic Chem Ind Co Ltd | Fluid mixing apparatus |
| CN202199281U (en) * | 2011-08-16 | 2012-04-25 | 甘肃华羚酪蛋白股份有限公司 | Automatic acid-mixing device |
| CN202823287U (en) * | 2012-08-23 | 2013-03-27 | 靖江市盛达环保设备有限公司 | Automation acid preparation equipment |
| CN103521123A (en) * | 2013-10-11 | 2014-01-22 | 长兴埃克森科技有限公司 | Automatic preparation system for dilute sulfuric acid |
| CN205095694U (en) * | 2015-10-16 | 2016-03-23 | 重庆华强生态肥业有限公司 | Hierarchical diluting device of concentrated sulfuric acid |
| CN205731094U (en) * | 2016-06-21 | 2016-11-30 | 佛山市安齿生物科技有限公司 | A kind of configuration system for the mixing of high concentration strong acid |
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Address after: 616850 Haitang Battery Industrial Park, Ganluo County, Liangshan Yi Autonomous Prefecture, Sichuan Province Applicant after: Sichuan Ols New Energy Technology Co., Ltd. Address before: 616850 Haitang Battery Industrial Park, Ganluo County, Liangshan Yi Autonomous Prefecture, Sichuan Province Applicant before: Sichuan Hezhong People's Livelihood New Energy Technology Co., Ltd. |
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