CN110006022A - A kind of high-field electrode boiler - Google Patents
A kind of high-field electrode boiler Download PDFInfo
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- CN110006022A CN110006022A CN201910396389.9A CN201910396389A CN110006022A CN 110006022 A CN110006022 A CN 110006022A CN 201910396389 A CN201910396389 A CN 201910396389A CN 110006022 A CN110006022 A CN 110006022A
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- 239000007788 liquid Substances 0.000 claims abstract description 73
- 238000005192 partition Methods 0.000 claims abstract description 18
- 238000000151 deposition Methods 0.000 claims 1
- 238000010079 rubber tapping Methods 0.000 claims 1
- 230000015556 catabolic process Effects 0.000 abstract description 7
- 238000009423 ventilation Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000010586 diagram Methods 0.000 description 6
- 238000009833 condensation Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 239000012153 distilled water Substances 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
- F22B1/30—Electrode boilers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/22—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/18—Arrangement or mounting of grates or heating means
- F24H9/1809—Arrangement or mounting of grates or heating means for water heaters
- F24H9/1818—Arrangement or mounting of electric heating means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H2250/00—Electrical heat generating means
- F24H2250/10—Electrodes
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses two kinds of high-field electrode boilers, respectively horizontal high-pressure electrode boiler and vertical high-field electrode boiler, are related to boiler plant technical field.Partition is arranged by filling a certain amount of incoagulable gas in shell in the high-field electrode boiler, and the inner space of the shell is divided into upper space and lower space.The electrode is located at upper space, and the lower space not only fills the liquid of certain conductivity, incoagulable gas memory space when being also up.Incoagulable gas is stored in this when operating normally, seldom in the content of upper space, ensure that the exchange capability of heat of First Heat Exchanger.Ventilation channel for being connected to the upper space and lower space is provided between the upper space and lower space, for liquid back pipe road, the high-field electrode boiler improves breakdown voltage by filling incoagulable gas, it avoids that arcing electric discharge occurs, the high-field electrode boiler can be recycled for multiple times after once filling incoagulable gas, be not necessarily to frequent inflation/deflation.
Description
Technical field
The present invention relates to boiler plant technical field, specifically a kind of high-field electrode boiler.
Background technique
In recent years due to being influenced by economic downlink, the ground winter such as power demand slowdown in growth, especially northeast and Xinjiang
Heating Period peak load regulation network is difficult, and abandonment abandoning optical phenomenon is serious, and electricity supply and demand is particularly thorny.Traditional coal heating system pollutant row
It puts seriously, winter haze is caused to lock city.It is in all parts of the country gradually to eliminate middle and small burn coal boiler, electric clean energy resource is changed using coal.
High-field electrode boiler is a kind of powering device of high efficiency no pollution, and the high-voltage electricity of 6-35kv is inserted directly into centainly
In the water of conductivity, water had not only done resistance but also had done heat transfer medium, and water is heated to be steam or high-temperature water, is supplied and is used by heat exchange equipment
Family uses.
There is following both sides in traditional high-field electrode boiler:
First, it is easy breakdown medium on startup, arcing electric discharge occurs.
Second, traditional high-field electrode boiler be solve the problems, such as incoagulable gas that arcing is filled with when operating normally, it is past
Toward needing that (especially steam type high-field electrode boiler) is discharged, the heat transfer effect for influencing heat exchanger is avoided.
Summary of the invention
In view of the above-mentioned problems, the high-field electrode boiler is not coagulated by filling the present invention provides a kind of high-field electrode boiler
Property gas improve breakdown voltage, avoid medium breakdown, occur arcing electric discharge.At the same time, lower space of the present invention is also
Incoagulable gas stores space, and when normal operation, incoagulable gas is stored in this, the content of incoagulable gas in upper space
Seldom, it ensure that the exchange capability of heat of First Heat Exchanger.Still further provide a kind of horizontal high-field electrode boiler, the horizontal height
Pressure electrode boiler not only passes through filling incoagulable gas and improves breakdown voltage, avoids medium breakdown, and arcing electric discharge occurs, and
And previous vertical structure is changed, expand the scope of application.
The technical scheme adopted by the invention to solve the technical problem is that:
A kind of high-field electrode boiler, the shell placed vertically including one are provided with electrode, the shell in the shell
It is filled with incoagulable gas in vivo, the inner space of the shell is divided into upper space and lower space by partition, described
Electrode is located at upper space, and the center of circle of the electrode in the horizontal plane about the shell is arranged symmetrically；
It is located above the electrode in the upper space and is provided with First Heat Exchanger, is contained in the lower space
It is placed with the liquid with certain conductivity；
Be provided on the shell exhaust passage for being connected to the upper space and lower space, liquid feeding pipeline and
Liquid back pipe road, circulating pump is provided on the liquid feeding pipeline, and the liquid back pipe road is provided with control valve.
Further, the exhaust passage is communicating exhaust gas pipe, and the upper port of the communicating exhaust gas pipe is positioned at described
The top of electrode.
Further, the gas vent being connected with the lower space is provided on the shell.
Further, the second heat exchanger is provided in the lower space.
A kind of high-field electrode boiler, including shell are provided with electrode in the shell, and the shell is horizontal positioned,
And incoagulable gas is filled in the shell, the inner space of the shell is divided into upper space and lower part empty by partition
Between；
The left end of the upper space is provided with null electrode cylinder, and the electrode is set in the null electrode cylinder, and
The center of circle of the electrode in the horizontal plane about the null electrode cylinder is arranged symmetrically, and the right end of the upper space is provided with
One heat exchanger is contained with the liquid with certain conductivity in the lower space；
The row for being connected to the upper space and lower space is provided between the upper space and lower space
Gas channel, liquid feeding pipeline and liquid back pipe road, circulating pump is provided on the liquid feeding pipeline, and the liquid back pipe road is provided with
Control valve.
Further, be provided with the gas vent being connected with the lower space on the shell, and it is described under
The second heat exchanger is provided in portion space.
Further, the exhaust passage be communicating exhaust gas pipe, and the communicating exhaust gas pipe be located at be provided with first
One end of heat exchanger.
Further, the left end of the partition has the recessed portion for storing liquid, and the null electrode cylinder is set to
In the recessed portion.
Further, the exhaust passage is the air vent being set on the partition.
Further, a liquid distribution plate is provided in the recessed portion, be provided on the liquid distribution plate circular through hole and
Baffle, and the circular through hole, baffle and null electrode cylinder three are coaxially arranged.
The beneficial effects of the present invention are:
1, by filling incoagulable gas in shell, so that breakdown voltage when boiler startup is higher than operating voltage, avoid
Arcing electric discharge.
2, when operating normally, incoagulable gas is stored in lower space, and incoagulable gas is seldom in upper space, ensure that
The exchange capability of heat of First Heat Exchanger.
3, it can be once recycled for multiple times after filling incoagulable gas, be not necessarily to frequent inflation/deflation, reduce the damage to equipment
Harmful and incoagulable gas dosage.
4, boiler built-in heat exchanger, it is compact-sized, reduce pipeline arrangement, space occupied and equipment investment, enhances and set
Standby using flexible.
5, by the way that the second heat exchanger is arranged in the top of lower space, to be carried out to a small amount of steam for entering lower space
Condensation, to guarantee incoagulable gas well into lower space.
6, another not in shell using the shell of ground connection as null electrode cylinder for vertical high-field electrode boiler
Null electrode cylinder is set, simplifies boiler structure, completely eliminates limitation of the null electrode cylinder to steam production, keep boiler efficiency higher,
Load Regulation is faster.
7, traditional high-field electrode boiler is typically all vertical, and height is generally at four meters or more, the layer of routine building object
Height is unable to satisfy requirement, is restricted in the scope of application, for horizontal high-field electrode boiler, changes previous
Vertical structure, be no longer influenced by the limitation of building storey height, be conducive to promote the use of.
8, for horizontal high-field electrode boiler, by the way that liquid distribution plate is arranged, to keep the distilled water being condensed back equal
In the recessed portion of even inflow partition, guarantee the solution concentration uniformity in recessed portion, avoids three-phase electricity consumption uneven.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of embodiment one；
Fig. 2 is the distributed architecture schematic diagram of electrode；
Fig. 3 is the structural schematic diagram of embodiment two；
Fig. 4 is the structural schematic diagram of embodiment three；
Fig. 5 is the structural schematic diagram of example IV；
Fig. 6 is the structural schematic diagram of embodiment five.
In figure: 1- shell, 2- electrode, 3- partition, 41- communicating exhaust gas pipe, 42- air vent, 51- First Heat Exchanger, 52-
Two heat exchangers, 61- liquid feeding pipeline, 611- circulating pump, 62- liquid back pipe road, 7- null electrode cylinder, 8- gas vent, 9- liquid distribution plate, 91-
Baffle.
Specific embodiment
Embodiment one
As shown in Figure 1, a kind of high-field electrode boiler includes a shell 1 placed vertically, and it is filled in the shell 1
A certain amount of incoagulable gas.As a kind of specific embodiment, incoagulable gas described in the present embodiment is nitrogen.It is described
Shell 1 in be provided with a partition 3, and the inner space of the shell 1 is divided into upper space and lower part by the partition 3
Space.
First Heat Exchanger 51 and electrode 2 are disposed in the upper space from top to bottom, and described first is changed
Hot device 51 and electrode 2 are fixedly connected with the shell 1 respectively.The inlet and outlet of the First Heat Exchanger 51 are respectively positioned on
The outside of the shell 1.
As a kind of specific embodiment, as shown in Figure 1, the shell of First Heat Exchanger described in the present embodiment and boiler
Shell, which is fixedly connected, together forms a unified cavity, and the heat exchanger tube of the heat exchanger extends in the shell of boiler.
As shown in Fig. 2, electrode 2 described in three is arranged at an equal altitude, and the center of circle in the horizontal plane about the shell 1 is symmetrical
Arrangement.It is sequentially connected the projection of the electrode 2 in the horizontal plane and forms equilateral triangle, and the geometric center of the equilateral triangle
On the axis of the shell 1.
A certain amount of liquid with certain conductivity is contained in the lower space.
As shown in Figure 1, be provided between the upper space and lower space for by the upper space not
Solidifying property gas is discharged into the exhaust passage of lower space.
As a kind of specific embodiment, exhaust passage described in the present embodiment is communicating exhaust gas pipe 41, and the row
The upper port of gas communicating pipe 41 is located at the top of the electrode 2.
As a kind of specific embodiment, as shown in Figure 1, the upper port of communicating exhaust gas pipe described in the present embodiment 41 and institute
The lower part for stating the shell of First Heat Exchanger is connected.
Liquid feeding pipeline 61 and liquid back pipe road 62, and the feed flow are additionally provided between the upper space and lower space
The upper port on pipeline 61 and liquid back pipe road 62 is connected with the lower end of the upper space respectively, the liquid feeding pipeline 61 and time liquid
The lower port of pipeline 62 is connected with the lower end of the lower space respectively.Circulating pump is provided on the liquid feeding pipeline 61
611, the control valve for controlling 62 on-off of liquid back pipe road is provided on the liquid back pipe road 62.
Further, in order to avoid boiler superpressure, the upper end of the lower space is provided with gas vent 8.
Further, described in order to guarantee that incoagulable gas well into lower space, guarantees the exchange capability of heat of heat exchanger
Lower space in be provided with the second heat exchanger 52, second heat exchanger 52 is fixedly connected with the shell 1, and described
The inlet and outlet of second heat exchanger 52 are respectively positioned on the outside of the shell 1.
It is provided with liquidometer in the upper space and lower space, is not regarded out in figure.
When boiler brings into operation, first by circulating pump 611 by the liquid pumping to upper space in lower space, so
After power on, starting trouble.The liquid of upper space is heated generation steam, since the density of steam is less than incoagulability gas
Body, therefore the steam generated can be according to from top to bottom, the rule from centre to surrounding is spread.With the generation of steam, top is empty
Interior pressure increase, First Heat Exchanger start to condense the steam in mixed gas, and incoagulable gas can pass through communicating exhaust gas pipe
41 are pressed into lower space, so that incoagulable gas be avoided to be collected at First Heat Exchanger 51, influence First Heat Exchanger 51
Heat transfer effect.The steam of generation can carry out heat exchange with First Heat Exchanger 51, and the condensed water generated after steam condensation can be returned directly
It falls in the liquid of upper space.By communicating exhaust gas pipe 41 enter lower space in a small amount of steam then with the second heat exchanger 52
Heat exchange is carried out, the distilled water generated after steam condensation is directly fallen back in the liquid of lower space.First Heat Exchanger 51 and
Two heat exchangers 52 can be connected according to actual requirement or parallel connection.
When boiler needs out of service, firstly, opening the control valve on liquid back pipe road 62, the liquid in upper space is in weight
It is back in lower space under the action of power, the liquid level in upper space gradually reduces, and the power of boiler also declines therewith.Work as pot
When the power of furnace drops to certain value, power supply is closed, boiler stops working.In this way primarily to avoiding powering off suddenly, electric current
Change dramatically impacts route.After boiler stops working, the pressure of upper space reduces, incoagulable gas due to pressure difference from
Hair returns to upper space.
Embodiment two
Outside in the upper space positioned at the electrode is provided with null electrode cylinder, and the electricity described in the horizontal plane
Pole is arranged symmetrically about the center of circle of the null electrode cylinder, remaining structure is the same as embodiment one.
Embodiment three
As shown in figure 3, a kind of high-field electrode boiler includes a horizontal positioned shell 1, and it is filled in the shell 1
A certain amount of incoagulable gas.As a kind of specific embodiment, nitrogen in incoagulable gas described in the present embodiment.It is described
Shell 1 in be provided with a partition 3, and the inner space of the shell 1 is divided into upper space and lower part by the partition 3
Space.
The left end of the upper space is provided with the rounded null electrode cylinder 7 in section, is provided in the null electrode cylinder 7
Electrode 2.The null electrode cylinder 7 and electrode 2 is fixedly connected with the shell 1 respectively.The high cloth such as electrode 2 described in three
It sets, and the center of circle about the null electrode cylinder 7 is arranged symmetrically in the horizontal plane.It is sequentially connected the electrode 2 in the horizontal plane
Projection form equilateral triangle, and the geometric center of the equilateral triangle is located on the axis of the null electrode cylinder 7.
The right end of the upper space is provided with First Heat Exchanger 51, the First Heat Exchanger 51 and the shell 1
It is fixedly connected, and the inlet and outlet of the First Heat Exchanger 51 are respectively positioned on the outside of the shell 1.
As a kind of specific embodiment, as shown in figure 3, the shell of First Heat Exchanger described in the present embodiment and boiler
Shell, which is fixedly connected, together forms a unified cavity, and the heat exchanger tube of the heat exchanger extends in the shell of boiler.
A certain amount of liquid with certain conductivity is contained in the lower space.
As shown in figure 3, being provided between the upper space and lower space for being connected to the upper space under
The exhaust passage in portion space.
As a kind of specific embodiment, exhaust passage described in the present embodiment is communicating exhaust gas pipe 41, and described
The upper end of communicating exhaust gas pipe 41 is connected with the lower part of the shell of the First Heat Exchanger 51.
Liquid feeding pipeline 61 and liquid back pipe road 62, and the feed flow are additionally provided between the upper space and lower space
The upper port on pipeline 61 and liquid back pipe road 62 is connected with the lower end of the upper space respectively, the liquid feeding pipeline 61 and time liquid
The lower port of pipeline 62 is connected with the lower end of the lower space respectively.Circulating pump is provided on the liquid feeding pipeline 61
611, the control valve for controlling 62 on-off of liquid back pipe road is provided on the liquid back pipe road 62.
Further, in order to avoid boiler superpressure, the upper end of the lower space is provided with gas vent 8.
Further, in order to guarantee making full use of for heat, the second heat exchanger 52, institute are provided in the lower space
The second heat exchanger 52 stated is fixedly connected with the shell 1, and the equal position of inlet and outlet of second heat exchanger 52
In the outside of the shell 1.
Preferably, second heat exchanger 52 is located at the same end of the shell 1 with the First Heat Exchanger 51.
It is provided with liquidometer in the upper space and lower space, is not regarded out in figure.
When boiler brings into operation, first by circulating pump 611 by the liquid pumping to upper space in lower space, so
After power on, starting trouble.The liquid of upper space is heated generation steam, since the density of steam is less than incoagulability gas
Body, therefore the steam generated can be according to from top to bottom, rule from left to right is spread.With the generation of steam, in upper space
Pressure increase, First Heat Exchanger start condense mixed gas in steam incoagulable gas can be pressed by communicating exhaust gas pipe 41
Enter in lower space, so that incoagulable gas be avoided to be collected at First Heat Exchanger 51, influences the heat exchange effect of First Heat Exchanger 51
Fruit.The steam of generation can carry out heat exchange with First Heat Exchanger 51, and the distilled water generated after steam condensation can directly be fallen back to
In the liquid in portion space.Heat then is carried out with the second heat exchanger 52 by a small amount of steam that communicating exhaust gas pipe 41 enters in lower space
Exchange, the distilled water generated after steam condensation are directly fallen back in the liquid of lower space.First Heat Exchanger 51 and the second heat exchange
Device 52 can be connected according to actual requirement or parallel connection.
When boiler needs out of service, firstly, opening the control valve on liquid back pipe road 62, the liquid in upper space is in weight
It is back in lower space under the action of power, the liquid level in upper space gradually reduces, and the power of boiler also declines therewith.Work as pot
When the power of furnace drops to certain value, power supply is closed, boiler stops working.In this way primarily to avoiding powering off suddenly, electric current
Change dramatically impacts route.After boiler stops working, the pressure of upper space reduces, incoagulable gas due to pressure difference from
Hair returns to upper space.
Example IV
As shown in figure 4, the left end of the partition 3 has one for storing the recessed portion of liquid, the null electrode cylinder 7 is set
It is placed in the recessed portion, remaining structure is the same as embodiment two.
As a kind of specific embodiment, partition 3 described in the present embodiment successively includes horizontally disposed from left to right
First transverse slat and the second transverse slat, and the height of first transverse slat is lower than second transverse slat, the right end of first transverse slat
One entirety is connected to become by riser with the left end of the second transverse slat.
Embodiment five
As shown in figure 5, the exhaust passage is the air vent 42 being set on the partition 3, and the air vent
42 are located on second transverse slat, the same example IV of remaining structure.
Embodiment six
As shown in fig. 6, be fixedly installed a liquid distribution plate 9 in the recessed portion, and the height of the liquid distribution plate 9 is less than etc.
In the height of second transverse slat.A circular through hole for being used to accommodate the null electrode cylinder 7 is provided on the liquid distribution plate 9,
And the circular through hole and the null electrode cylinder 7 are coaxial, the diameter of the circular through hole is greater than the straight of the null electrode cylinder 7
Diameter.Baffle 91 annular in shape, and the baffle 91 and the coaxial cloth of circular through hole are provided on the liquid distribution plate 9
It sets, remaining structure is same
Embodiment five.
In this way, the condensed water being condensed back can flow on liquid distribution plate 9 first, and gather on liquid distribution plate 9, until the cloth
Liquid level on liquid plate 9 reaches the height of the baffle 91, the condensed water in liquid distribution plate 9 will cross baffle 91 uniformly flow into it is recessed
In concave portion, to guarantee solution concentration uniformity in recessed portion, avoid density unevenness that arcing is caused to discharge.
Claims (10)
1. a kind of high-field electrode boiler, the shell placed vertically including one is provided with electrode in the shell, and feature exists
In: incoagulable gas is filled in the shell, the inner space of the shell is divided into upper space and lower part by partition
Space, the electrode is located at upper space, and the electrode is arranged symmetrically about the shell center of circle in the horizontal plane；
It is located above the electrode in the upper space and is provided with First Heat Exchanger, is contained in the lower space
Liquid with certain conductivity；
It is provided with the exhaust passage for being connected to the upper space and lower space, liquid feeding pipeline on the shell and returns liquid
Pipeline, circulating pump is provided on the liquid feeding pipeline, and the liquid back pipe road is provided with control valve.
2. a kind of high-field electrode boiler according to claim 1, it is characterised in that: the exhaust passage is communicating exhaust gas
Pipe, and the upper port of the communicating exhaust gas pipe is located at the top of the electrode.
3. a kind of high-field electrode boiler according to claim 1, it is characterised in that: be provided on the shell with it is described
The gas vent that is connected of lower space.
4. a kind of high-field electrode boiler according to claim 1, it is characterised in that: is provided in the lower space
Two heat exchangers.
5. a kind of high-field electrode boiler, including shell, electrode is provided in the shell, it is characterised in that: the shell
It is horizontal positioned, and incoagulable gas is filled in the shell, the inner space of the shell is divided into top empty by partition
Between and lower space；
The left end of the upper space is provided with null electrode cylinder, and the electrode is set in the null electrode cylinder, and described
The center of circle of the electrode in the horizontal plane about the null electrode cylinder be arranged symmetrically, the right end of the upper space is provided with first and changes
Hot device is contained with the liquid with certain conductivity in the lower space；
The exhaust being provided between the upper space and lower space for being connected to the upper space and lower space is logical
Road, liquid feeding pipeline and liquid back pipe road, circulating pump is provided on the liquid feeding pipeline, and the liquid back pipe road is provided with control
Valve.
6. a kind of high-field electrode boiler according to claim 5, it is characterised in that: be provided on the shell with it is described
The gas vent that is connected of lower space, and the second heat exchanger is provided in the lower space.
7. a kind of high-field electrode boiler according to claim 5, it is characterised in that: the exhaust passage is communicating exhaust gas
Pipe, and the communicating exhaust gas pipe is located at the one end for being provided with First Heat Exchanger.
8. a kind of high-field electrode boiler according to claim 5, it is characterised in that: the left end of the partition has for depositing
The recessed portion of tapping body, the null electrode cylinder are set in the recessed portion.
9. a kind of high-field electrode boiler according to claim 8, it is characterised in that: the exhaust passage is is set to
State the air vent on partition.
10. a kind of high-field electrode boiler according to claim 8, it is characterised in that: one is provided in the recessed portion
Liquid distribution plate is provided with circular through hole and baffle, and circular through hole, baffle and the null electrode cylinder three on the liquid distribution plate
It is coaxially arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910396389.9A CN110006022B (en) | 2019-05-14 | 2019-05-14 | High-voltage electrode boiler |
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|---|---|---|---|
| CN201910396389.9A CN110006022B (en) | 2019-05-14 | 2019-05-14 | High-voltage electrode boiler |
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| CN110006022A true CN110006022A (en) | 2019-07-12 |
| CN110006022B CN110006022B (en) | 2024-01-05 |
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| CN201910396389.9A Active CN110006022B (en) | 2019-05-14 | 2019-05-14 | High-voltage electrode boiler |
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2019
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|---|---|---|---|---|
| GB642862A (en) * | 1948-08-14 | 1950-09-13 | James Mcdonald | Improvements in electrode boilers |
| KR20110061986A (en) * | 2009-12-02 | 2011-06-10 | 황보기철 | Hot air blower combined with boiler using electric arc reactor device |
| CN105080177A (en) * | 2015-09-14 | 2015-11-25 | 李永堂 | Efficient separation and vacuum condensation system for non-condensable gas |
| CN205909499U (en) * | 2016-06-30 | 2017-01-25 | 陕西龙源电气科工贸有限公司 | High voltage (10~35Kv) electrode boiler |
| CN206235004U (en) * | 2016-11-09 | 2017-06-09 | 北京瑞特爱能源科技股份有限公司 | One kind can expand power formula normal pressure electrode boiler |
| CN206449622U (en) * | 2016-12-28 | 2017-08-29 | 杭州华源前线能源设备有限公司 | Electric pole type hot-water boiler circulation process system |
| CN108692455A (en) * | 2018-07-17 | 2018-10-23 | 天津宝成机械制造股份有限公司 | A kind of high-field electrode hot water boiler system |
| CN209960454U (en) * | 2019-05-14 | 2020-01-17 | 山东北辰机电设备股份有限公司 | High-voltage electrode boiler |
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| CN110006022B (en) | 2024-01-05 |
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