CN205746787U - A kind of New-type boiler feedwater deaeration equipment - Google Patents
A kind of New-type boiler feedwater deaeration equipment Download PDFInfo
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- CN205746787U CN205746787U CN201620618769.4U CN201620618769U CN205746787U CN 205746787 U CN205746787 U CN 205746787U CN 201620618769 U CN201620618769 U CN 201620618769U CN 205746787 U CN205746787 U CN 205746787U
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- deoxygenation
- reaction chamber
- boiler
- water
- tank
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Abstract
The utility model discloses a kind of New-type boiler feedwater deaeration equipment, including feed-tank, water tank and deoxygenation reaction chamber is placed after being divided into deoxygenation in feed-tank, place after deoxygenation between water tank and deoxygenation reaction chamber by converting pipeline connection, convert and be provided with an electromagnetic valve on pipeline, the bottom of deoxygenation reaction chamber is provided with electric boiling plate, the top of deoxygenation reaction chamber is provided with inlet channel, oxygen scavenger placing box and steam channel, it is provided with on inlet channel and controls electromagnetic valve into water, oxygen scavenger placing box is connected by oxygen scavenger conveyance conduit and deoxygenation reaction chamber, oxygen scavenger transfer solenoid valve it is provided with on oxygen scavenger conveyance conduit, oxygen sensor it is provided with in steam channel.This kind of New-type boiler feedwater deaeration equipment, easy to use, simple to operate, it is easily controlled, thermal loss is little, and production cost is low, and deaerating effect is reliable.
Description
Technical field
This utility model relates to a kind of deaeration plant, particularly to a kind of New-type boiler feedwater deaeration equipment, belongs to machinery
Apparatus field.
Background technology
In boiler feedwater processes technical process, deoxygenation is a link of non-the normally off key.Oxygen is the feed water system of boiler
Main corrosion material, the oxygen in water supply system should rapidly be removing, and otherwise it can corrode water supply system and the portion of boiler
Part, corrosive substance ferrum oxide can enter in boiler, deposits or be attached on boiler tube wall and heating surface, forms indissoluble and conducts heat
Bad ferrum dirt, the ferrum dirt of corrosion can cause inner-walls of duct appearance point to cheat, and resistance coefficient increases.When corrosive pipeline is serious, even
Pipeline explosion accident can occur.National regulation evaporation capacity more than or equal to the steam boiler of two tphs and water temperature more than or equal to 95
DEG C hot-water boiler all must deoxygenation.But existing boiler deoxidizing method equipment, in use, operation complexity, it is not easy to control, heat
Amount loss is big, and production cost is high, and deaerating effect is unreliable.
Utility model content
The technical problems to be solved in the utility model is to overcome existing boiler deoxidizing method equipment, in use, and operation complexity, no
Being easily controlled, thermal loss is big, and production cost is high, the insecure defect of deaerating effect, it is provided that a kind of New-type boiler feedwater deaeration
Equipment, thus solve the problems referred to above.
In order to solve above-mentioned technical problem, this utility model provides following technical scheme:
This utility model one New-type boiler feedwater deaeration equipment, including feed-tank, after being divided into deoxygenation in described feed-tank
Place water tank and deoxygenation reaction chamber, place after described deoxygenation between water tank and described deoxygenation reaction chamber by converting pipeline connection, institute
Stating and be provided with an electromagnetic valve on conversion pipeline, the bottom of described deoxygenation reaction chamber is provided with electric boiling plate, and described deoxygenation is reacted
The top of case is provided with inlet channel, oxygen scavenger placing box and steam channel, described inlet channel is provided with and controls electricity into water
Magnet valve, described oxygen scavenger placing box is connected by oxygen scavenger conveyance conduit and described deoxygenation reaction chamber, described oxygen scavenger conveying pipe
Being provided with oxygen scavenger transfer solenoid valve on road, be provided with oxygen sensor in described steam channel, the avris of described feed-tank is arranged
There is control chamber, be provided with single-chip microcomputer and accumulator in described control chamber, described control chamber is provided with data display screen and operation
Button.
As a kind of optimal technical scheme of the present utility model, described feed-tank bottom connects boiler aqueduct, institute
Stating and be provided with boiler water delivery electromagnetic valve on boiler aqueduct, described boiler aqueduct and boiler connect, the end of described boiler
Portion is provided with weight sensor, and the water after deoxygenation can be made to be directly entered in boiler, it is to avoid the dissolving again of oxygen is penetrated into, convenient
The water demand of boiler, water consumption is controlled, it is simple to the use of boiler.
As a kind of optimal technical scheme of the present utility model, place in water tank and described deoxygenation reaction chamber after described deoxygenation
It is provided with level sensor, level sensor can be passed through, place in water tank and deoxygenation reaction chamber after being directly acquainted with deoxygenation
SEA LEVEL VARIATION, it is simple to the grasp going out oxygen progress.
As a kind of optimal technical scheme of the present utility model, the avris of described control chamber is provided with temperature controller, can
To control the water temperature in deoxygenation reaction chamber, facilitate deoxygenation.
Compared with prior art, the beneficial effects of the utility model are: this kind of New-type boiler feedwater deaeration equipment, by setting
The steam channel put, it is possible to release the oxygen in deoxygenation reaction chamber, by the oxygen sensor arranged, it is possible to detect accurately and remove
The oxygen content of oxygen reaction chamber, it is simple to understand deoxygenation degree in deoxygenation reaction chamber, by placing water tank after the deoxygenation of setting, it is possible to
Store the water yield after deoxygenation, it is ensured that the lasting water consumption of boiler, by the inlet channel arranged and oxygen scavenger placing box, it is possible to from
Dynamic discharging water deoxygenation reaction chamber and oxygen scavenger takes, convenient reaction, by the single-chip microcomputer arranged, it is possible to by various signals
Process, it is achieved automatization, this kind of New-type boiler feedwater deaeration equipment, easy to use, simple to operate, it is easily controlled, heat
Losing little, production cost is low, and deaerating effect is reliable.
Accompanying drawing explanation
Accompanying drawing is used for providing being further appreciated by of the present utility model, and constitutes a part for description, with this practicality
Novel embodiment is used for explaining this utility model together, is not intended that restriction of the present utility model.In the accompanying drawings:
Fig. 1 is structural representation of the present utility model；
In figure: 1, boiler；2, boiler aqueduct；3, boiler water delivery electromagnetic valve；4, feed-tank；5, accumulator；6, temperature
Controller；7, operation button；8, data display screen；9, single-chip microcomputer；10, electric boiling plate；11, deoxygenation reaction chamber；12, oxygen scavenger is defeated
Send pipeline；13, oxygen scavenger transfer solenoid valve；14, oxygen scavenger placing box；15, inlet channel；16, water inlet controls electromagnetic valve；17、
Steam channel；18, oxygen sensor；19, level sensor；20, an electromagnetic valve；21, pipeline is converted；22, water is placed after deoxygenation
Case；23, weight sensor；24, control chamber.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment, based on the embodiment in this utility model, those of ordinary skill in the art are not under making creative work premise
The every other embodiment obtained, broadly falls into the scope of this utility model protection.
Refer to Fig. 1, the open a kind of technical scheme of this utility model: a kind of New-type boiler feedwater deaeration equipment, including to
Water tank 4, places water tank 22 and deoxygenation reaction chamber 11 after being divided into deoxygenation in feed-tank 4, places water tank 22 and deoxygenation reaction after deoxygenation
Being connected by conversion pipeline 21 between case 11, convert and be provided with an electromagnetic valve 20 on pipeline 21, the bottom of deoxygenation reaction chamber 11 sets
Being equipped with electric boiling plate 10, the top of deoxygenation reaction chamber 11 is provided with inlet channel 15, oxygen scavenger placing box 14 and steam channel 17,
Being provided with on inlet channel 15 and control electromagnetic valve 16 into water, oxygen scavenger placing box 14 is anti-by oxygen scavenger conveyance conduit 12 and deoxygenation
Answer case 11 to connect, oxygen scavenger conveyance conduit 12 is provided with oxygen scavenger transfer solenoid valve 13, aerobic is set in steam channel 17 and passes
Sensor 18, the avris of feed-tank 4 is provided with control chamber 24, is provided with single-chip microcomputer 9 and accumulator 5, control chamber 24 in control chamber 24
On be provided with data display screen 8 and operation button 7.Feed-tank 4 bottom connects has boiler aqueduct 2, on boiler aqueduct 2
Being provided with boiler water delivery electromagnetic valve 3, boiler aqueduct 2 and boiler 1 to connect, the bottom of boiler 1 is provided with weight sensor 23,
The water after deoxygenation can be made to be directly entered in boiler 1, it is to avoid the dissolving again of oxygen is penetrated into, and facilitates the water demand of boiler 1, use
The water yield is controlled, it is simple to the use of boiler 1.It is provided with level sensor in placing water tank 22 and deoxygenation reaction chamber 11 after deoxygenation
19, level sensor 19 can be passed through, after being directly acquainted with deoxygenation, place the SEA LEVEL VARIATION in water tank 22 and deoxygenation reaction chamber 11,
It is easy to the grasp going out oxygen progress.The avris of control chamber 24 is provided with temperature controller 6, can control in deoxygenation reaction chamber 11
Water temperature, facilitates deoxygenation, by releasing the oxygen in deoxygenation reaction chamber.
During use, can be arranged in single-chip microcomputer 9 by operation button 7 and use water weight amount, deoxygenation reaction chamber in boiler 1
Oxygen content numerical value in 11, places the peak level in water tank 22 and deoxygenation reaction chamber 11 and lowest water level numerical value after deoxygenation,
After setting completes, opened by single-chip microcomputer 9 and control electromagnetic valve 16 into water, deoxygenation reaction chamber 11 is discharged water, when water level reaches
Specific bit postpones, and is received by level sensor 19, delivers a signal to single-chip microcomputer 9, after single-chip microcomputer 9 receives signal, closes water inlet
Controlling electromagnetic valve 16, electric boiling plate 10, under the temperature of temperature controller 6 controls, is heated, at this moment manual unlocking oxygen scavenger
Transfer solenoid valve 13, puts into a certain amount of oxygen scavenger, carries out deoxygenation, by steam channel 17, it is possible to release in deoxygenation reaction chamber
Oxygen, when the oxygen in deoxygenation reaction chamber 11 less than setting value time, received by oxygen sensor 18, deliver a signal to single-chip microcomputer 9,
Single-chip microcomputer 9 can open conversion pipeline 21, makes the water after deoxygenation place in water tank 22, when the water of deoxygenation reaction chamber 11 after entering deoxygenation
When position is less than setting value, conversion pipeline 21 can be closed, when boiler 1 needs to use water, boiler water delivery electromagnetic valve 3 can be opened, to pot
Stove 1 feeds water, and after the weight of water arrives and specifies numerical value, is received by weight sensor 23, delivers a signal to single-chip microcomputer 9, single
Sheet machine 9 can cut out boiler water delivery electromagnetic valve 3.
This kind of New-type boiler feedwater deaeration equipment, by the steam channel arranged, it is possible to release the oxygen in deoxygenation reaction chamber
Gas, by the oxygen sensor arranged, it is possible to detect the oxygen content of deoxygenation reaction chamber accurately, it is simple to understand deoxygenation reaction chamber
Interior deoxygenation degree, places water tank by after the deoxygenation that arranges, it is possible to store the water yield after deoxygenation, it is ensured that the continuing of boiler uses water
Amount, by the inlet channel arranged and oxygen scavenger placing box, it is possible to automatically discharge water deoxygenation reaction chamber and oxygen scavenger is put
Taking, convenient reaction, by the single-chip microcomputer arranged, it is possible to being processed by various signals, it is achieved automatization, this kind of New-type boiler is given
Water deaeration plant, easy to use, simple to operate, it is easily controlled, thermal loss is little, and production cost is low, and deaerating effect is reliable.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, it is not limited to this
Utility model, although being described in detail this utility model with reference to previous embodiment, for those skilled in the art
For, the technical scheme described in foregoing embodiments still can be modified by it, or to wherein portion of techniques feature
Carry out equivalent, all within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, all
Within protection domain of the present utility model should be included in.
Claims (4)
1. a New-type boiler feedwater deaeration equipment, including feed-tank (4), it is characterised in that be divided in described feed-tank (4) and removing
Place water tank (22) and deoxygenation reaction chamber (11) after oxygen, place between water tank (22) and described deoxygenation reaction chamber (11) after described deoxygenation
Connect by converting pipeline (21), described conversion pipeline (21) is provided with an electromagnetic valve (20), described deoxygenation reaction chamber
(11) bottom is provided with electric boiling plate (10), and the top of described deoxygenation reaction chamber (11) is provided with inlet channel (15), deoxygenation
Agent placing box (14) and steam channel (17), described inlet channel (15) is provided with and controls electromagnetic valve (16) into water, described remove
Oxygen agent placing box (14) is connected by oxygen scavenger conveyance conduit (12) and described deoxygenation reaction chamber (11), described oxygen scavenger conveying pipe
It is provided with oxygen scavenger transfer solenoid valve (13) on road (12), in described steam channel (17), is provided with oxygen sensor (18), described
The avris of feed-tank (4) is provided with control chamber (24), is provided with single-chip microcomputer (9) and accumulator (5), institute in described control chamber (24)
State and on control chamber (24), be provided with data display screen (8) and operation button (7).
A kind of New-type boiler feedwater deaeration equipment the most according to claim 1, it is characterised in that described feed-tank (4) end
End connection has boiler aqueduct (2), and described boiler aqueduct (2) is provided with boiler water delivery electromagnetic valve (3), described boiler
Aqueduct (2) and boiler (1) connect, and the bottom of described boiler (1) is provided with weight sensor (23).
A kind of New-type boiler feedwater deaeration equipment the most according to claim 1, it is characterised in that place water after described deoxygenation
It is provided with level sensor (19) in case (22) and described deoxygenation reaction chamber (11).
A kind of New-type boiler feedwater deaeration equipment the most according to claim 1, it is characterised in that described control chamber (24)
Avris is provided with temperature controller (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620618769.4U CN205746787U (en) | 2016-06-22 | 2016-06-22 | A kind of New-type boiler feedwater deaeration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620618769.4U CN205746787U (en) | 2016-06-22 | 2016-06-22 | A kind of New-type boiler feedwater deaeration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205746787U true CN205746787U (en) | 2016-11-30 |
Family
ID=57383939
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620618769.4U Expired - Fee Related CN205746787U (en) | 2016-06-22 | 2016-06-22 | A kind of New-type boiler feedwater deaeration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205746787U (en) |
-
2016
- 2016-06-22 CN CN201620618769.4U patent/CN205746787U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161130 Termination date: 20180622 |