CN217785114U - Constant-speed spray deaerator - Google Patents
Constant-speed spray deaerator Download PDFInfo
- Publication number
- CN217785114U CN217785114U CN202221570865.8U CN202221570865U CN217785114U CN 217785114 U CN217785114 U CN 217785114U CN 202221570865 U CN202221570865 U CN 202221570865U CN 217785114 U CN217785114 U CN 217785114U
- Authority
- CN
- China
- Prior art keywords
- oxygen
- eliminating
- chamber
- water
- deoxidization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Physical Water Treatments (AREA)
Abstract
The utility model discloses a constant speed spraying oxygen-eliminating device, including deoxidization water tank and oxygen-eliminating tower, the oxygen-eliminating tower is installed at the top of deoxidization water tank, gas-water separator is installed on the top of oxygen-eliminating tower, the blast pipe is installed at gas-water separator's top, the inside top of oxygen-eliminating tower is equipped with third oxygen-eliminating chamber, the membrane ware is installed at the top of third oxygen-eliminating chamber, the inlet tube is installed to the one end of membrane ware, the basin of depositing is installed to the bottom of membrane ware, the bottom of third oxygen-eliminating chamber is equipped with second oxygen-eliminating chamber, all install a plurality of spraying board on the inside both sides of second oxygen-eliminating chamber, this oxygen-eliminating device can carry out the oxygen-gas separation many times in the aquatic, thereby reach the purpose of quick deoxidization, the deoxidization is efficient, and fast, stable in structure reduces the oxygen content in the aquatic, thereby protect the boiler, water supply pipe and economizer, the steam that adopts in this oxygen-eliminating device comes from the boiler, resource rational utilization, reduce the deoxidization cost, make things convenient for people to use.
Description
Technical Field
The utility model relates to a deaerator field specifically is a constant speed spraying deaerator.
Background
The deaerator is one of the key equipment of boiler and heating system, if the deaerator has poor deaerating capacity, the serious loss caused by the corrosion to the boiler water supply pipeline, the coal economizer and other accessory equipment, the caused economic loss is dozens or hundreds of times of the deaerator cost, the existing deaerator has single function, often the deaerating efficiency is low, the deaerating effect is poor, the oxygen content in water exceeds the standard, and the existing deaerator does not adopt the mode of constant-speed spraying to deaerate, so that the contact time of steam and water is short, and the oxygen in the water cannot be effectively separated, therefore, the constant-speed spraying deaerator is provided.
Disclosure of Invention
The utility model aims at the defect of prior art, provide a constant speed spraying oxygen-eliminating device to solve the problem that above-mentioned background art provided.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a constant-speed spraying deaerator, includes deoxidization water tank and deoxidization tower, the deoxidization tower is installed at the top of deoxidization water tank, deareator is installed on the top of deoxidization tower, the blast pipe is installed at deareator's top, the inside top of deoxidization tower is equipped with third deoxidization room, the membrane ware has been installed at the top of third deoxidization room, the inlet tube is installed to the one end of membrane ware, the bottom of membrane ware is installed and is deposited the basin, the bottom of third deoxidization room is equipped with second deoxidization room, all install a plurality of spraying plate on the inside both sides of second deoxidization room, all link to each other through the link between every spraying plate, the bottom of third deoxidization room is equipped with first deoxidization room, the internally mounted of first deoxidization room has the trickle grate, thermal storage filler liquid steam net is installed to the bottom of trickle grate, the centrifugal pump is installed to top one side of deoxidization water tank, the thermometer is installed to one side of centrifugal pump, be connected with the deoxidization pipe on the water tank, the top of deoxidization pipe is connected with the overflow pipe, the bottom of deoxidization pipe is installed the water level the deoxidization water tank, the bottom of deoxidization water tank, the base is installed, the water level drain pipe.
As an optimal technical scheme of the utility model, the both sides of second oxygen-eliminating chamber all link to each other with third oxygen-eliminating chamber through steam exhaust pipe, gas-water separator passes through the bolt and installs on the top of oxygen-eliminating tower, the blast pipe passes through the bolt and installs on gas-water separator's top.
As an optimal technical scheme of the utility model, it installs on the inside of third oxygen-eliminating chamber to play membrane ware through the bolt, the basin that deposits passes through the bolt and installs on the inside bottom of third oxygen-eliminating chamber.
As a preferred technical scheme of the utility model, the spraying board passes through the bolt and installs on the both sides of second oxygen-eliminating chamber, the link passes through the bolt and installs between two spraying boards, the mid-mounting of link has the second connecting pipe, links to each other through the second connecting pipe between two spraying boards, install the filter screen on the link.
As a preferred technical scheme of the utility model, the centrifugal pump links to each other with basin and spraying plate through first connecting pipe respectively, heat accumulation filler liquid steam net and trickle comb are all installed on the inside of first oxygen-eliminating chamber through the bolt.
As a preferred technical scheme of the utility model, bottom one side of first oxygen-eliminating chamber, second oxygen-eliminating chamber and third oxygen-eliminating chamber all is connected with steam conveying pipe, the base welding is on the bottom of deoxidization water tank, the water level pipe adopts the transparent PVC material to make.
The utility model has the advantages that: this oxygen-eliminating device can carry out the oxygen of aquatic and separate many times to reach the purpose of quick deoxidization, the deoxidization is efficient, and is fast, and stable in structure reduces the oxygen content of aquatic, thereby protection boiler, water supply pipe and economizer, and the steam that adopts in this oxygen-eliminating device comes from the boiler, and resource rational utilization reduces the deoxidization cost, makes things convenient for people to use.
Drawings
Fig. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic structural view of the connection frame of the present invention.
In the figure: the device comprises a deoxidizing water tank 1, a deoxidizing tower 2, a first deoxidizing chamber 3, a second deoxidizing chamber 4, a third deoxidizing chamber 5, a water inlet pipe 6, a steam discharging pipe 7, a steam conveying pipe 8, a film lifting device 9, a gas-water separator 10, an exhaust pipe 11, a water storage tank 12, a spraying plate 13, a first connecting pipe 14, a centrifugal pump 15, a water level pipe 16, an overflow pipe 17, a water discharging pipe 18, a base 19, a thermometer 20, a connecting frame 21, a heat storage filler liquid-vapor net 22, a water spraying grate 23, a second connecting pipe 24 and a filter screen 25.
Detailed Description
The following detailed description of the preferred embodiments of the present invention will be provided in conjunction with the accompanying drawings, so that the advantages and features of the present invention can be more easily understood by those skilled in the art, and the protection scope of the present invention can be clearly and clearly defined.
Example (b): referring to fig. 1-2, the present invention provides a technical solution: the utility model provides a constant speed spraying oxygen-eliminating device, including deoxidization water tank 1 and deoxidization tower 2, deoxidization tower 2 is installed at deoxidization water tank 1's top, gas-water separator 10 is installed on deoxidization tower 2's top, blast pipe 11 is installed at gas-water separator 10's top, deoxidization tower 2's inside top is equipped with third deoxidization room 5, play membrane ware 9 is installed at the top of third deoxidization room 5, it installs inlet tube 6 to play membrane ware 9's one end, it installs water storage tank 12 to play membrane ware 9's bottom, the bottom of third deoxidization room 5 is equipped with second deoxidization room 4, all install a plurality of spraying board 13 on the inside both sides of second deoxidization room 4, all link to each other through link 21 between every spraying board 13, the bottom of third deoxidization room 5 is equipped with first deoxidization room 3, the internally mounted of first deoxidization room 3 has a trickle grate 23, thermal storage filler vapour net 22 is installed to the bottom of trickle grate 23, centrifugal pump 15 is installed to top one side of centrifugal pump 15, be connected with water level pipe 16 on deoxidization 1, the top of deoxidization pipe 16 is connected with water tank 17, deoxidization water tank 19 the bottom of deoxidization water tank is installed to deoxidization water tank, deoxidization tank 18 drain pipe.
The both sides of second oxygen-eliminating chamber 4 all link to each other with third oxygen-eliminating chamber 5 through steam exhaust pipe 7, and gas-water separator 10 passes through the bolt and installs on the top of oxygen-eliminating tower 2, and blast pipe 11 passes through the bolt and installs on gas-water separator 10's top.
The membrane remover 9 is mounted on the inside of the third deoxygenation chamber 5 by bolts, and the water storage tank 12 is mounted on the bottom end of the inside of the third deoxygenation chamber 5 by bolts.
The spraying plates 13 are installed on two sides of the second deaerating chamber 4 through bolts, the connecting frame 21 is installed between the two spraying plates 13 through bolts, the second connecting pipe 24 is installed in the middle of the connecting frame 21, the two spraying plates 13 are connected through the second connecting pipe 24, and the connecting frame 21 is provided with the filter screen 25.
The centrifugal pump 15 is respectively connected with the water storage tank 12 and the spraying plate 13 through a first connecting pipe 14, and the heat storage filler liquid-vapor net 22 and the water spraying grate 23 are both installed on the inner part of the first deaerating chamber 3 through bolts.
Bottom one side of first oxygen-eliminating chamber 3, second oxygen-eliminating chamber 4 and third oxygen-eliminating chamber 5 all is connected with steam delivery pipe 8, and base 19 welds on the bottom of deoxidization water tank 1, and water level pipe 16 adopts transparent PVC material to make.
The working principle is as follows: a constant-speed spray deaerator comprises a deaerating water tank 1, a deaerating tower 2, a first deaerating chamber 3, a second deaerating chamber 4 and a third deaerating chamber 5, when in use, water enters a membrane-lifting device 9 through a water inlet pipe 6, the membrane-lifting device 9 adopts a membrane-lifting device for a rotary membrane deaerator, steam is conveyed into the membrane-lifting device 9 through a steam conveying pipe 8, the water in the membrane-lifting device 9 is contacted with the steam, partial oxygen in the water is separated, the water after the oxygen is separated flows into a water storage tank 12, the water in the water storage tank 12 is sucked into spray plates 13 through a centrifugal pump 15 for electrifying work, the water is conveyed into the spray plates 13 through a second connecting pipe 24, fog is sprayed out through the spray plates 13, then the steam is conveyed through the steam conveying pipe 8 on the second deaerating chamber 4, the fog is contacted with the steam, and partial oxygen in the fog is taken away, oxygen and steam are conveyed to the top of the deoxidizing tower 2 through a steam discharging pipe 7, fog sprayed out through a spraying plate 13 finally falls onto a water spraying grate 23, water is sprayed onto a heat storage filler liquid-steam net 22 through the water spraying grate 23, then steam is conveyed to the top of the deoxidizing tower 2 through a steam conveying pipe 8 on a first deoxidizing chamber 3 to be in contact with water on the heat storage filler liquid-steam net 22, partial oxygen is separated again, the steam and the oxygen in the first deoxidizing chamber 3 enter a second deoxidizing chamber 4 together, then the steam and the oxygen are conveyed to the top of the deoxidizing tower 2 through the steam discharging pipe 7 from the second deoxidizing chamber 4, then the steam and the water are separated through a gas-water separator 10, and then the separated gas is discharged through an exhaust pipe 11, so that the oxygen in the water is quickly and effectively separated and taken away through a multi-stage separation mode, the oxygen content in the water in the deoxidizing water tank 1 is reduced, and the water level in the deoxidizing water tank 1 is visually seen through a water level pipe 16, when the water is excessive, the water can be discharged by using the overflow pipe 17, so that the sufficient water in the deoxygenated water tank 1 is ensured.
This oxygen-eliminating device can carry out the oxygen of aquatic and separate many times to reach the purpose of quick deoxidization, the deoxidization is efficient, and is fast, and stable in structure reduces the oxygen content of aquatic, thereby protection boiler, water supply pipe and economizer, and the steam that adopts in this oxygen-eliminating device comes from the boiler, and resource rational utilization reduces the deoxidization cost, makes things convenient for people to use.
The above embodiments only represent several embodiments of the present invention, and the description thereof is specific and detailed, but not to be construed as limiting the scope of the present invention. It should be noted that, for those skilled in the art, without departing from the spirit of the present invention, several variations and modifications can be made, which are within the scope of the present invention.
Claims (6)
1. The utility model provides a constant speed spraying oxygen-eliminating device, includes deoxidization water tank (1) and oxygen-eliminating tower (2), its characterized in that: the oxygen-eliminating tower (2) is installed at the top of the oxygen-eliminating water tank (1), a gas-water separator (10) is installed on the top of the oxygen-eliminating tower (2), an exhaust pipe (11) is installed at the top of the gas-water separator (10), a third oxygen-eliminating chamber (5) is arranged on the top of the oxygen-eliminating tower (2), a membrane device (9) is installed at the top of the third oxygen-eliminating chamber (5), a water inlet pipe (6) is installed at one end of the membrane device (9), a water storage tank (12) is installed at the bottom of the membrane device (9), a second oxygen-eliminating chamber (4) is arranged at the bottom of the third oxygen-eliminating chamber (5), a plurality of spraying plates (13) are installed on two sides of the interior of the second oxygen-eliminating chamber (4), all link to each other through link (21) between every spraying board (13), the bottom of third oxygen-eliminating chamber (5) is equipped with first oxygen-eliminating chamber (3), the internally mounted of first oxygen-eliminating chamber (3) has water drenching grate (23), heat accumulation filler liquid steam net (22) is installed to the bottom of water drenching grate (23), centrifugal pump (15) are installed to top one side of deoxidization water tank (1), thermometer (20) are installed to one side of centrifugal pump (15), be connected with water level pipe (16) on deoxidization water tank (1), the top of water level pipe (16) is connected with overflow pipe (17), base (19) are installed to the bottom of deoxidization water tank (1), drain pipe (18) are installed to the bottom of deoxidization water tank (1).
2. The constant-speed spray deaerator of claim 1, characterized in that: the both sides of second oxygen-eliminating chamber (4) all link to each other with third oxygen-eliminating chamber (5) through steam exhaust pipe (7), gas-water separator (10) are installed on the top of oxygen-eliminating tower (2) through the bolt, blast pipe (11) are installed on the top of gas-water separator (10) through the bolt.
3. The constant-speed spray deaerator of claim 1, characterized in that: the film forming device (9) is installed on the inside of the third deaerating chamber (5) through bolts, and the water storage tank (12) is installed at the bottom end of the inside of the third deaerating chamber (5) through bolts.
4. The constant-speed spray deaerator of claim 1, characterized in that: the spraying plate (13) is installed on two sides of the second deaerating chamber (4) through bolts, the connecting frame (21) is installed between the two spraying plates (13) through bolts, a second connecting pipe (24) is installed in the middle of the connecting frame (21), the two spraying plates (13) are connected through the second connecting pipe (24), and the connecting frame (21) is provided with a filter screen (25).
5. The constant-speed spray deaerator of claim 1, characterized in that: the centrifugal pump (15) is respectively connected with the water storage tank (12) and the spraying plate (13) through a first connecting pipe (14), and the heat storage filler liquid-vapor net (22) and the water spraying grate (23) are both installed on the inner portion of the first deaerating chamber (3) through bolts.
6. The constant-speed spray deaerator of claim 1, characterized in that: bottom one side of first oxygen-eliminating chamber (3), second oxygen-eliminating chamber (4) and third oxygen-eliminating chamber (5) all is connected with steam delivery pipe (8), base (19) welding is on the bottom of deoxidization water tank (1), water level pipe (16) adopt transparent PVC material to make.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221570865.8U CN217785114U (en) | 2022-06-22 | 2022-06-22 | Constant-speed spray deaerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221570865.8U CN217785114U (en) | 2022-06-22 | 2022-06-22 | Constant-speed spray deaerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217785114U true CN217785114U (en) | 2022-11-11 |
Family
ID=83937436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221570865.8U Active CN217785114U (en) | 2022-06-22 | 2022-06-22 | Constant-speed spray deaerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217785114U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116105122A (en) * | 2022-12-26 | 2023-05-12 | 连云港市宏庆电力辅机开发有限公司 | Analytic deaerator |
-
2022
- 2022-06-22 CN CN202221570865.8U patent/CN217785114U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116105122A (en) * | 2022-12-26 | 2023-05-12 | 连云港市宏庆电力辅机开发有限公司 | Analytic deaerator |
| CN116105122B (en) * | 2022-12-26 | 2023-09-22 | 连云港市宏庆电力辅机开发有限公司 | Analytic deaerator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN217785114U (en) | Constant-speed spray deaerator | |
| CN109959017B (en) | Boiler waste liquid blending combustion device | |
| CN210544337U (en) | Secondary waste gas desulfurization box | |
| CN215916528U (en) | Three-phase separation system for tar, ammonia water and tar residues | |
| CN205815453U (en) | A kind of tripolyphosphate sodium polymerization tail gas recovery device | |
| CN207520857U (en) | A kind of desulfuration absorbing tower device | |
| CN201458785U (en) | Purified acid wastewater degasser | |
| CN212119539U (en) | Heat recovery sulphur removal device | |
| CN211098184U (en) | Electroplating workshop exhaust treatment system | |
| CN203954713U (en) | Vacuum unit with the rectifying column of gas and oil separating plant | |
| CN205832877U (en) | Flue gas processing device with Water spray function | |
| CN209481574U (en) | The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene | |
| CN210718813U (en) | Waste gas waste heat recovery indirect heating equipment convenient to wash | |
| CN212102077U (en) | Water seal voltage stabilizer | |
| CN208465513U (en) | A kind of smoldering furnace emission-control equipment | |
| CN217662534U (en) | High-efficient energy-conserving desulfurization dust collecting equipment | |
| CN207605494U (en) | A kind of gas water removal oil removing multicore filter | |
| CN219156559U (en) | Permeate heating device | |
| CN212537806U (en) | Novel multi-functional low level is arranged heating power oxygen-eliminating device | |
| CN215996153U (en) | Hydrochloric acid tail gas treatment system for oil-containing substances | |
| CN205269355U (en) | Waste gas purification apparatus | |
| CN104791822A (en) | Multi-layer parallel-connection overlaid frame type spraying flue gas waste heat recovery and heat exchange device | |
| CN213778613U (en) | Tunnel cave SOx/NOx control tower | |
| CN216986995U (en) | Double-tangential inlet absorption tower port | |
| CN214972754U (en) | Double-layer horizontal slag pit dust removing tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |