CN106894883B - A kind of expansion tank and processing method - Google Patents
A kind of expansion tank and processing method Download PDFInfo
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- CN106894883B CN106894883B CN201710113086.2A CN201710113086A CN106894883B CN 106894883 B CN106894883 B CN 106894883B CN 201710113086 A CN201710113086 A CN 201710113086A CN 106894883 B CN106894883 B CN 106894883B
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- expansion tank
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- built
- ion
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- 238000003672 processing method Methods 0.000 title claims abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 239000002826 coolant Substances 0.000 claims abstract description 36
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000000945 filler Substances 0.000 claims abstract description 24
- 229910052742 iron Inorganic materials 0.000 claims abstract description 19
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000013022 venting Methods 0.000 claims abstract description 10
- 239000002253 acid Substances 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 6
- 239000000523 sample Substances 0.000 claims description 27
- 230000000694 effects Effects 0.000 claims description 14
- 150000002500 ions Chemical class 0.000 claims description 13
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 12
- 239000003957 anion exchange resin Substances 0.000 claims description 10
- 239000003729 cation exchange resin Substances 0.000 claims description 10
- 239000002131 composite material Substances 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 8
- 238000007789 sealing Methods 0.000 claims description 8
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 claims description 7
- 229910001425 magnesium ion Inorganic materials 0.000 claims description 7
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 claims description 6
- 229910001424 calcium ion Inorganic materials 0.000 claims description 6
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 claims description 6
- -1 iron ion Chemical class 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 5
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 238000005259 measurement Methods 0.000 claims description 3
- 238000005341 cation exchange Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims description 2
- 230000008961 swelling Effects 0.000 claims 1
- 238000001816 cooling Methods 0.000 abstract description 31
- 238000010521 absorption reaction Methods 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 5
- 230000009471 action Effects 0.000 abstract description 4
- 238000002955 isolation Methods 0.000 abstract description 4
- 230000002085 persistent effect Effects 0.000 abstract description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052791 calcium Inorganic materials 0.000 abstract description 2
- 239000011575 calcium Substances 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 10
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical group OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- 230000017525 heat dissipation Effects 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 239000000383 hazardous chemical Substances 0.000 description 3
- 238000005349 anion exchange Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 230000002045 lasting effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000012954 risk control Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/02—Liquid-coolant filling, overflow, venting, or draining devices
- F01P11/029—Expansion reservoirs
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/02—Liquid-coolant filling, overflow, venting, or draining devices
- F01P11/0276—Draining or purging
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/02—Liquid-coolant filling, overflow, venting, or draining devices
- F01P11/028—Deaeration devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/06—Cleaning; Combating corrosion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/14—Indicating devices; Other safety devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/14—Indicating devices; Other safety devices
- F01P11/18—Indicating devices; Other safety devices concerning coolant pressure, coolant flow, or liquid-coolant level
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/06—Cleaning; Combating corrosion
- F01P2011/061—Cleaning or combating corrosion using filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
- F01P11/06—Cleaning; Combating corrosion
- F01P2011/066—Combating corrosion
- F01P2011/068—Combating corrosion chemically
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P2050/00—Applications
- F01P2050/22—Motor-cars
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The present invention relates to a kind of expansion tank and processing method, including expansion tank shell, kettle end cap, expansion tank shell inner route clapboard is divided into first chamber and second chamber;Close filler, pressure cover, radiator exhaust water pipe head, engine exhaust water pipe head, engine refill adapter, venting conduit, exhaust manifolds and built-in core are provided on kettle end cap.The technical program passes through the intracorporal two chambers of expansion tank shell and a built-in core, pass through level-one Physical Absorption, isolation and second level, three-level chemical action, iron rust, scale, bubble and the potential threats such as reaction treatment calcium and magnesium iron ion and acid ion generated in absorption cooling system work, maintain coolant liquid pH value constant, for system output cleaning, the coolant liquid of safety, so that it is guaranteed that cooling system secure persistent efficient operation, complete vehicle fault rate is reduced and with vehicle cost.
Description
Technical field
The invention belongs to engine-cooling system technical field, a kind of expansion tank and processing method are particularly related to.
Background technique
According to investigations, the automobile engine source of failure in 50% or more the whole world is in cooling system.Engine is at work
A large amount of heat can be generated, after indicating oven temperature of engine, will lead to its efficiency is reduced, even Parts Breakdown.Automobile
The circulation that cooling system passes through pipeline and access progress liquid in engine.Heat can be absorbed when liquid flows through high-temperature engine
Amount, reduces the temperature of engine, provides temperature appropriate to guarantee that engine is in a suitable operating temperature.Liquid flows through
After engine, then heat exchanger (radiator) is flowed to, the heat in liquid is dispersed into air by heat exchanger.But automobile
After a period of use, often there is oil consumption increase, water temperature is easy higher, or even alarm " boiling ", and expansion tank is smudgy,
The problems such as not seeing liquid level, engine scuffing when serious, especially diesel-engine road vehicle.Leading to this failure cause is vehicle cooling system
System is enclosed cooling water heat exchange work system, and the hazardous substances such as iron rust, scale unavoidably generated in work can not be timely
It is discharged to outside system, blocks pipeline, cause cooling system heat dissipation bad, cause engine overheat, the thermal efficiency reduces, and oil consumption increases;
Coolant liquid main component is ethylene glycol, and high-temperature oxydation can generate acidic materials, PH is caused to reduce, and corrodes engine, transports for a long time
Row certainly will influence engine life and user's value.
Summary of the invention
The object of the present invention is to provide a kind of expansion tank and processing methods, are being worked with solving prior art expansion tank
The hazardous substances such as middle scale can not the problem of discharge system is outer and cooling corrosion engine.
The present invention is achieved by the following technical solutions:
A kind of expansion tank, including expansion tank shell, kettle end cap, the expansion tank shell inner route clapboard are divided into
First chamber and second chamber;
Kettle ending cover hole, the kettle end cap are provided with the first chamber corresponding position on the expansion tank shell
It is fixed on the kettle ending cover hole by locking nut, filler is provided on the kettle end cap, the filler is logical
The sealing of excess pressure lid;
Be provided on the expansion tank shell of the first chamber upper side radiator exhaust water pipe head and
Engine exhaust water pipe head;
Engine refill adapter is provided with below the expansion tank shell to be connected to the second chamber;
One end of venting conduit is set to the filler close at the expansion tank shell, and connects with the filler
Logical, the other end of the relief tube is connected to the second chamber;
The upper end of exhaust manifolds is connected to the filler, and the other end is in communication with the outside, and the exhaust manifolds add described
The position of geat is higher than the relief tube in the position of the filler;
Built-in core is provided in the first chamber;The lower end of the built-in core offsets with the partition, with
Communicating pipe is provided at the opposite partition in the lower end of the built-in core;
Differential pressure pickup, first pressure probe, second pressure probe and pH sensor are provided on the kettle end cap
Probe, the first pressure probe and second pressure probe are electrically connected with the differential pressure pickup;
The first pressure probe is provided in first chamber, and the second pressure probe and the pH sensor control head are equal
It is set in the built-in core.
It is provided with highest calibration points and minimum calibration points on the expansion tank shell, and connects with the second chamber
It is logical;The upper surface of the built-in core is lower than the highest calibration points, and the lower end surface of the built-in core is lower than the minimum quarter
Degree point.
It is provided with the first drainage plate at the nearly radiator exhaust water pipe head in the expansion tank shell, described
The second drainage plate is provided with above built-in core.
The built-in core is conical tube structure, and the outer diameter of upper end is less than the outer diameter of lower end, the lower end of the built-in core
Outer diameter is less than the diameter of the kettle ending cover hole.
The built-in core successively includes M type high molecular composite filtering paper layer, anion exchange resin layer and sun from the outside to the core
Ion exchange resin layer.
The volume of the cation exchange resin layer is fill coolant liquid total measurement (volume) 4/3000ths to thousand/1000ths;It is described
The volume of anion exchange resin layer is twice of the cation exchange resin layer.
Relief valve is provided in the relief tube;The position of the relief valve is lower than the position of the pressure cover inner seal ring
It sets.
A kind of processing method of expansion tank, uses the expansion tank of any of the above-described, comprising the following steps:
1) level-one acts on, be absorbed by M type high molecular composite filtering paper layer iron rust in first chamber, scale and every
From bubble;
2) second level act on, by anion exchange resin layer dispose into the acid ion etc. in first chamber endanger from
Son, and generate hydroxyl ion;
3) three-level acts on, and is disposed by cation exchange resin layer into calcium ion, magnesium ion, the iron in first chamber
Ion etc. endangers ion and generates hydrogen ion;
4) the poly- hydroxyl ion 2) of step and the poly- hydrogen ion chemical reaction 3) of step generate deionized water.
The beneficial effects of the present invention are:
The technical program is inhaled by the intracorporal two chambers of expansion tank shell and a built-in core by level-one physics
It receives, isolation and second level, three-level chemical action, iron rust, scale, bubble and the reaction treatment calcium generated in absorption cooling system work
The potential threats such as magnesium ion, iron ion, acid ion maintain coolant liquid pH value constant, for system output cleaning, the cooling of safety
Liquid, so that it is guaranteed that cooling system secure persistent efficient operation, substantially reduces complete vehicle fault rate and user with vehicle cost.
By disposing iron rust, scale and potentially hazardous ion, it is ensured that cooling system secure persistent efficient operation reduces
Oil consumption and complete vehicle fault rate.
By separation bubble, cooling system heat dissipation performance is promoted, expansion tank blooming and Parts Breakdown are avoided the occurrence of;
By being managed to the coolant liquid and the double-deck of supplement coolant liquid that enter in expansion tank, the coolant liquid in externally fill and system
Risk is handled, and guarantees that the coolant liquid for whenever entering engine is all cleaning, safety, full maintenance cooling system
And engine.
User is substantially reduced with vehicle cost.Without going to the professional shop 4S, high expense, cleaning cooling system water channel, replacement are spent
Coolant liquid.Need to only spend very low expense replace expansion tank just can essence exclude risk, easy to operate, oneself can also start
Replacement.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of expansion tank of the present invention;
Fig. 2 is the schematic diagram of internal structure of expansion tank of the present invention;
Fig. 3 is expansion tank coolant injection schematic diagram of the present invention;
Fig. 4 is relief valve closed mode schematic diagram;
Fig. 5 is expansion tank internal work schematic diagram;
Fig. 6 is pressure release the valve opening state schematic diagram;
Fig. 7 is built-in core cross-sectional schematic diagram;
Fig. 8 is built-in core coagulation schematic diagram;
Fig. 9 is built-in core two stage treatment schematic diagram;
Figure 10 is built-in core tertiary treatment schematic diagram.
Description of symbols
1 expansion tank shell, 2 radiators are vented water pipe head, and 3 engine exhaust water pipe heads, 4 exhaust manifolds, 5 start
Machine refill adapter, 6 first pressures probe, 7 locking nuts, 8 differential pressure pickups, 9 kettle end caps, 10 second pressures probe, 11
Pressure cover, 12 fillers, 13 venting conduits, 14 highest calibration points, 15 minimum calibration points, 16 first drainage plates, 17 first chambers,
Core built in 18,19 partitions, 20 communicating pipes, 21 second chambers, 22 kettle ending cover holes, 23 relief valves, 24 sealing rings, 25 end caps are close
Seal, 26M type high molecular composite filtering paper layer, 27 anion exchange resin layers, 28 cation exchange resin layers, 29 second drainages
Plate, 30pH sensor probe.
Specific embodiment
Carry out the technical solution that the present invention will be described in detail by the following examples, embodiment below is merely exemplary, only
It can be used to explanation and illustration technical solution of the present invention, and be not to be construed as the limitation to technical solution of the present invention.
The effect of the expansion tank of the application:
Derusting, scale removal: it by iron rust, the scale generated in high molecular composite filtering paper layer Physical Absorption cooling system, keeps away
Exempt from that blocking pipe phenomenon occurs, guarantees that heat dissipation performance high efficiency plays, while reducing oil consumption.
It excludes potential risk: by cation and anion exchange chemical action, before forming iron rust, scale, removing coolant liquid
In calcium ions and magnesium ions and iron ion and deionized water needed for forming system, avoid the later period from forming the potential risk of iron rust, scale,
System work is set to be constantly in secure high performance operating status.
Deacidification: by anion exchange chemical action, the acid ion of ethylene glycol high-temperature oxydation generation is displaced, makes to cool down
Liquid pH value maintains always ideal range, avoids coolant liquid acidizing corrosion engine water jacket, excludes the risk of engine scuffing.
It avoids Parts Breakdown: being not in the smudgy problem of expansion tank scale wall built-up and sensor fault.
Bubble separation, noise reduction and heat radiation performance: absorbing the high temperature and pressure bubble during air-discharging, and output is stable
Water flow prevents bubble explosion, reduces noise, promotes expansion tank reliability and system radiating performance, while evading cavitation erosion risk.
Least risk: source control initially fills coolant liquid, enters back into after first passing around expansion tank core tertiary treatment
Engine operation, for engine input cleaning coolant liquid, problem is controlled from source, by cooling system work in risk control
System is in minimum zone.
Cost is reduced, user satisfaction is promoted: need to only spend very low expense to regularly replace expansion tank, and not have to spend big valence
Money cleans water channel, is also not thorough.User is greatly reduced with vehicle cost, effect is more preferable.
The expansion tank of the technical program passes through level-one Physical Absorption, isolation and second level, three-level by built-in core
Effect, the iron rust generated in absorption cooling system work, scale, bubble and reaction treatment calcium ions and magnesium ions, iron ion, it is acid from
The potential threats such as son make coolant liquid pH value maintain suitable constant range, clean for system output, the coolant liquid of safety, with
Guarantee the safe and efficient lasting work of cooling system.
The application provides a kind of expansion tank, as shown in Figures 1 to 10, including expansion tank shell 1, kettle end cap 9, institute
It states expansion tank shell inner route clapboard 19 and is divided into first chamber 17 and second chamber 21.
Kettle ending cover hole 22, the kettle end are provided with the first chamber corresponding position on the expansion tank shell
Lid is fixed on the kettle ending cover hole by locking nut 7, is provided with end between the kettle end cap and kettle ending cover hole
Lid sealing ring 25, is provided with filler 12 on the kettle end cap, and the filler is sealed by pressure cover.Locking nut can
To unscrew, it is convenient for changing built-in core 18.
As depicted in figs. 1 and 2, radiator exhaust water pipe head 2 and engine exhaust water pipe head 3 are arranged in expansion tank
Left side top position of keeping to the side is connected to first chamber, and engine refill adapter 5 is arranged in expansion tank shell lower end surface, is located at
Radiator is vented the same side of water pipe head, is connected to second chamber.
Pressure cover and filler are rotatablely connected, and for closing filler, sealing ring 24 are provided on pressure cover, pressure release is led
One end of pipe 13 is set to the filler and is connected to close at the expansion tank shell, and with the filler, the pressure release
The other end of pipe is connected to second chamber.
Coolant liquid height identification, including highest calibration points 14 and minimum calibration points are provided on the right side of expansion tank shell
15。
The upper end of exhaust manifolds 4 is connected to the filler, and the other end is in communication with the outside, and the exhaust manifolds add described
The position of geat is located at relief tube higher than sealing ring of the relief tube on the position of the filler, pressure cover and leads with exhaust
Between pipe, the lower end of exhaust manifolds is vertically downward.
Built-in core 18 is provided in first chamber, the lower end of the built-in core offsets with the partition, with institute
Communicating pipe 20 is provided at the opposite partition in the lower end of core built in stating.
The upper surface of the built-in core is lower than the highest calibration points, the lower end surface of the built-in core lower than it is described most
Low scale point.
The built-in core is conical tube structure, and the outer diameter of upper end is less than the outer diameter of lower end, the lower end of the built-in core
Outer diameter is less than the diameter of kettle ending cover hole, and taking-up is facilitated to replace.
Differential pressure pickup 8, first pressure probe 6,10 and pH of second pressure probe is provided on the kettle end cap to pass
Sensor probe 30, the first pressure probe and second pressure probe are electrically connected with the differential pressure pickup.
The first pressure probe is provided in first chamber, and the second pressure probe and the pH sensor control head are equal
It is set in the built-in core.
First pressure probe is for the coolant pressure before monitoring processing, and second pressure probe is for monitoring by three-level
Coolant pressure after reason, differential pressure pickup can judge whether water resistance meets system requirements according to the two pressure difference, will when exceeded
It is alarmed by sensor connector feedback signal to ECU or instrument, user is reminded to replace in time.
Such as coolant liquid is acidified simultaneously, and pH sensor probe can output signal to warning device, and warning device can export difference
Signal reminds user's maintenance to ECU or instrument.
It is provided with the first drainage plate 16 at the nearly radiator exhaust water pipe head in the expansion tank shell, in institute
It states and is provided with the second drainage plate 29 above built-in core, be to prevent coolant liquid straight for protecting built-in core design
The built-in core of impact is connect, is damaged.
The function of first chamber is the danger handled in the coolant liquid newly filled and the coolant liquid recycled in cooling system work
Evil substance and separation bubble do not enter second chamber and participate in cooling cycle, it is ensured that cooling system safe and highly efficient operation.
Second chamber is connected to filler by venting conduit, and 23 position of relief valve in venting conduit is lower than pressure cover
Sealing ring position, the effect of second chamber are vented for engine moisturizing and cooling system.
The working principle of expansion tank
As shown in figure 3, the daily filling of coolant liquid, it is only necessary to open the filling that pressure cover carries out coolant liquid, coolant liquid is first
First chamber is reached, second chamber is entered by communicating pipe after the three-level effect of built-in core processing, is that cooling system is defeated
Send cleaning and the coolant liquid of safety.
Relief valve in venting conduit is in close state before not reaching setting pressure, as shown in figure 4, when filling
When coolant liquid exceeds the water level line below minimum calibration points, the pressure area of a sealing is formed in the top area A of second chamber, it is empty
Gas principle is to make the function of built-in core to guarantee upper surface of the cooling level in first chamber always above built-in core
Effect maximizes.
In this application, built-in core is similar conical tube structure, and the outer diameter of upper surface is less than the outer diameter of lower end surface, purpose
It is also the surface area and effect for promoting built-in core, plays the role of double shield.After filling, coolant liquid height control exists
Between highest calibration points and minimum calibration points.
In order to which expansion tank reaches constant lasting treatment effect, and maintain coolant liquid pH value in constant range, sun
The volume of ion exchange resin layer is that cooling system fills 4th/3000 to thousand/1000ths of coolant liquid total measurement (volume), anion exchange
Resin layer is necessary for twice of cation exchange resin layer volume.
When cooling system pressure reaches setup pressure value, relief valve and pressure cover in venting conduit can be opened successively,
As shown in fig. 6, expansion tank completes exhaust pressure relief work, after cooling system pressure reduction, relief valve and pressure cover can be closed successively
It closes.
Built-in core working principle:
Level-one effect absorbs iron rust, scale and separation bubble by M type high molecular composite filtering paper layer 26.
Second level effect, acid ion etc. is disposed by anion exchange resin layer 27 and endangers ion, and generate hydrogen-oxygen from
Son.
Three-level effect, disposes calcium ion, magnesium ion, iron ion etc. by cation exchange resin layer 28 and endangers ion simultaneously
Generate hydrogen ion.
When cooling system works, coolant liquid is vented water pipe head, engine exhaust water pipe head into the by radiator
After one cavity area, first passes around M type high molecular composite filtering paper layer and complete iron rust, scale absorption and bubble isolation (prevention bubble
Cooling water circulation is participated in, heat dissipation performance is improved), using anion exchange resin layer, ion-exchange treatment falls acid ion, most
Afterwards by cation exchange resin layer, fallen by ion exchange the calcium ion in coolant liquid, magnesium ion, iron ion etc. endanger from
Son.
After coolant liquid is by the above tertiary treatment, hazardous substance is all disposed, second level effect and three-level effect
Hydroxyl ion and the hydrogen ion chemical reaction generated afterwards generates the deionized water harmless to cooling system, it is ensured that cooling system can pacify
Full persistent high efficiency operation.
The above is only the descriptions of the preferred embodiment of the present invention, it is noted that due to the finiteness of literal expression, and
Objectively there is unlimited specific structure, for those skilled in the art, is not departing from the principle of the invention
Under the premise of, several improvements and modifications can also be made, these modifications and embellishments should also be considered as the scope of protection of the present invention.
Claims (8)
1. a kind of expansion tank, it is characterised in that: including expansion tank shell and kettle end cap, in the expansion tank shell by
Partition is divided into first chamber and second chamber;
Kettle ending cover hole is provided with the first chamber corresponding position on the expansion tank shell, the kettle end cap passes through
Locking nut is fixed on the kettle ending cover hole, and filler is provided on the kettle end cap, and the filler passes through pressure
The sealing of power lid;
It is provided with radiator exhaust water pipe head on the expansion tank shell of the first chamber upper side and starts
Machine is vented water pipe head;
Engine refill adapter is provided with below the expansion tank shell to be connected to the second chamber;
One end of venting conduit is set to the filler and is connected to close at the expansion tank shell, and with the filler,
The other end of the venting conduit is connected to the second chamber;
The upper end of exhaust manifolds is connected to the filler, and the other end is in communication with the outside, and the exhaust manifolds are in the filler
Position be higher than the relief tube in the position of the filler;
Built-in core is provided in the first chamber;The lower end of the built-in core offsets with the partition, with it is described
Communicating pipe is provided at the opposite partition in the lower end of built-in core;
Differential pressure pickup, first pressure probe, second pressure probe and pH sensor probe are provided on the kettle end cap,
The first pressure probe and second pressure probe are electrically connected with the differential pressure pickup;
The first pressure probe is provided in first chamber, and the second pressure probe and the pH sensor control head are respectively provided with
In in the built-in core.
2. expansion tank according to claim 1, it is characterised in that: be provided with highest quarter on the expansion tank shell
Degree point and minimum calibration points, and be connected to the second chamber;The upper surface of the built-in core is lower than the highest scale
The lower end surface of point, the built-in core is lower than the minimum calibration points.
3. expansion tank according to claim 1, it is characterised in that: the nearly radiator in the expansion tank shell
It is provided with the first drainage plate at exhaust water pipe head, is provided with the second drainage plate above the built-in core.
4. expansion tank according to claim 1, it is characterised in that: the built-in core is conical tube structure, upper end
Outer diameter is less than the outer diameter of lower end, and the lower end outer diameter of the built-in core is less than the diameter of the kettle ending cover hole.
5. expansion tank according to any one of claim 1 to 4, it is characterised in that: the built-in core is from the outside to the core
It successively include M type high molecular composite filtering paper layer, anion exchange resin layer and cation exchange resin layer.
6. expansion tank according to claim 5, it is characterised in that: the volume of the cation exchange resin layer is filling
4th/3000th to thousand/1000ths of coolant liquid total measurement (volume);The volume of the anion exchange resin layer is the cation exchange tree
Twice of rouge layer.
7. expansion tank according to claim 1, it is characterised in that: be provided with relief valve in the venting conduit;Institute
The position for stating relief valve is lower than the position of the pressure cover inner seal ring.
8. a kind of processing method of expansion tank, it is characterised in that: use the swelling water of any one of the claims 1 to 7
Pot, comprising the following steps:
1) simultaneously gas is isolated in level-one effect, the iron rust being absorbed into first chamber by M type high molecular composite filtering paper layer, scale
Bubble;
2) second level acts on, and is disposed by anion exchange resin layer into the acid ion in first chamber and endangers ion, and
Generate hydroxyl ion;
3) three-level acts on, and is disposed by cation exchange resin layer into calcium ion, magnesium ion, the iron ion in first chamber
It endangers ion and generates hydrogen ion;
4) the poly- hydroxyl ion 2) of step and the poly- hydrogen ion chemical reaction 3) of step generate deionized water.
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CN106894883B true CN106894883B (en) | 2019-02-19 |
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CN112297951B (en) * | 2020-09-15 | 2022-04-29 | 浙江中车电车有限公司 | Automobile-used cooling system with self-bleeding function |
CN112901332A (en) * | 2021-04-13 | 2021-06-04 | 河南柴油机重工有限责任公司 | Method for relieving cavitation erosion of diesel engine body |
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US4387671A (en) * | 1981-07-13 | 1983-06-14 | Jarvis Robert D | Air filter for a cooling system overflow container |
US4995452A (en) * | 1981-09-18 | 1991-02-26 | Minnesota Mining And Manufacturing Company | Filter-conditioner for motor cooling liquid |
US5111776A (en) * | 1989-09-26 | 1992-05-12 | Nippon Soken, Inc. | Cooling system for an internal combustion engine |
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