CN2651596Y - Automatic descaling and antiscaling DC boiler - Google Patents
Automatic descaling and antiscaling DC boiler Download PDFInfo
- Publication number
- CN2651596Y CN2651596Y CN 03248503 CN03248503U CN2651596Y CN 2651596 Y CN2651596 Y CN 2651596Y CN 03248503 CN03248503 CN 03248503 CN 03248503 U CN03248503 U CN 03248503U CN 2651596 Y CN2651596 Y CN 2651596Y
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Abstract
The utility model relates to an automatic scale-removing antiscale once-through boiler which comprises a water-feeding pump, a spiral heating pipe, a combustion device and a water control device; the utility model is characterized in that a set of liquid-solid separation distributor is arranged between a water inlet and a steam outlet of the spiral heating pipe of the once-through boiler, the liquid-solid separation distributor is composed of a separation settling chamber and a guide chamber, the top of the separation settling chamber is provided with a clear water outlet pipe communicated with a steam outlet of the boiler, the upper part of the separation settling chamber is provided with a fluid inlet pipe communicated with the steam outlet of the spiral heating pipe, the side of the guide chamber is respectively provided with a clear water inlet pipe and a mixed fluid outlet pipe, the clear water inlet pipe is communicated with the outlet of the water-feeding pump, the mixed fluid outlet pipe is communicated with the water inlet of the spiral heating pipe, the bottom of the guide chamber is provided with a drainage pipe, and the drainage pipe is communicated with a stop valve. The once-through boiler can conveniently and automatically remove scale, keep the inner wall of the evaporating pipe clean, and have no scale; as the once-through boiler has no requirements for the water quality, a water treating equipment is unnecessary to be set and the water quality is also unnecessary to be detected.
Description
Affiliated technical field
The utility model relates to a kind of steam generator, especially automatically the antiscaling, descaling direct current cooker.
Background technology
At present, known direct current cooker is meant that the feedwater of boiler relies on pressure once-through in heating surface of feed pump to produce the steam generation boiler of steam.This boiler is made up of feed pump, spiral tube heating surface (dividing radiation heating-surface and convection heating surface), burner and water controller.This boiler extracts hydraulic pressure by feed pump and goes into the spiral tube heating surface from water tank, spiral tube is at burner hearth and convection part is accepted fuel and air mixing after-combustion flame radiation is hot and the once pre-thermal evaporation of advection heat quilt is heated into steam, discharges from the stop valve of upper boiler.This boiler does not have jumbo drum and water drum, does not need to collect case yet.Its water capacity is generally all smaller, and the danger of its blast is also smaller, almost can ignore.Just owing to this, direct current cooker is very high to requirements in water quality, and well-known, the calcium that contains in the former water, magnesium ion composition have certain rigidity, be condensed on the evaporation tube in boiler into incrustation scale attached on the pipe inner wall, its result can cause water pipe heat transfer severe exacerbation.On the other hand, the thermal conductivity factor of incrustation scale only is 1/40~1/50 of an evaporation tube metal material, tube wall causes that because of adhering to incrustation scale the evaporation tube temperature rises, and the heat by tube wall will reduce, and surpasses the allowable temperature of material when the temperature of tube wall, the strength of materials will reduce, cause water pipe dilatancy even booster, not only cause the waste of boiler thermal output reduction and fuel, and water pipe booster rear furnace body is not easy maintenance, often need to change, thereby result in greater loss.Therefore all these type of boilers all are equipped with demineralizing plant both at home and abroad, and the hardness ions concentration of stove water is detected, and force to make the boiler periodical blowdown, regularly clean.Operation easier and operating cost have been increased.
Summary of the invention
In order to overcome the deficiency that existing direct current cooker is very high to water quality requirement, must set up hydrotreater, reduce the boiler acquisition cost, increase the boiler operatiopn effect, reduce operating cost, the utility model provides a kind of automatic desludging direct current cooker, and this direct current cooker can make things convenient for automatic desludging, keep the evaporation tube inwall clean, do not retain incrustation scale, water quality is not required, thereby need not to be provided with water treatment facilities and water quality is detected.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of automatic desludging antiscale direct current cooker, by feed pump, heat pipe spirals, burner and water controller are formed, the liquid-solid separating dispenser of installing one cover between the water inlet of the heat pipe that spirals of direct current cooker and venthole, this liquid-solid separating dispenser is made of separate and subside chamber and diversion chamber, top, separate and subside chamber is hollow cylinder, the bottom is a hollow cone, on, be connected between the bottom, at the top of separate and subside chamber the clear water output pipe is housed, the clear water output pipe is connected with the boiler gas outlet, fluid inlet tubes is equipped with on top in the separate and subside chamber, fluid inlet tubes is connected with the heat pipe gas outlet of spiraling, in the bottom of separate and subside chamber the particle control valve is housed, diversion chamber is a hollow cylinder body structure, its inside is provided with the baffle of a band tapering, at the top of diversion chamber the particle inlet tube is housed, the particle inlet tube is connected with the particle control valve outlet of bottom, separate and subside chamber, at other clear water inlet tube and the fluid-mixing outlet of also being equipped with respectively of the side of diversion chamber, the clear water inlet tube is connected with the feed pump outlet, the fluid-mixing outlet is connected with the heat pipe water inlet that spirals, blow-off pipe is equipped with in bottom in diversion chamber, and blow-off pipe is connected with a stop valve.
Boiler feed pump extracts water from water tank, at first enter the inlet port of liquid-solid separating dispenser bottom, because hydraulic action, the solids of liquid-solid separating dispenser inside are pressed into continuously the water inlet of the heat pipe that spirals from the outlet of liquid-solid separating dispenser bottom, flow along the spiral tube inwall, enter into the import on liquid-solid separating dispenser top from the outlet of spiral tube, because the change of flow direction and slowing down of speed, make solids different because of proportion with water, in liquid-solid separating dispenser, separate, water flows out from the delivery port on liquid-solid separating dispenser top, solids are deposited in the inside of liquid-solid separating dispenser and are deposited to its bottom and mix with the current that the bottom water inlet enters because of gravitational settling, are pressed into the water inlet of spiral tube with water, so go round and begin again, constantly circulation.
The know-why that the utility model technical solution problem is adopted is:
In the heat pipe that spirals, the solids of configuration certain particle size and volumetric concentration, in the certain flow scope under the drive of water, particle is mobile in pipe with the water of motion in pipe, solids constantly collide with inside pipe wall, thereby reach automatic cleaning and descaling, antiscale purpose.This device has two effects, and the one, the water that comes out from the spiral tube venthole and the fluid-mixing of solids are carried out liquid-solid the separation, solids are collected.The 2nd, the particle of collecting is sent into spiral tube again by water inlet.
The beneficial effects of the utility model are: can clean the inwall of the heat pipe that spirals of direct current cooker automatically, avoid inwall to produce incrustation scale, keep the efficient heat transfer effect of heat pipe, thereby reach the purpose that cuts down the consumption of energy.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1. be structural representation of the present utility model,
Fig. 2 is the structural representation of the liquid-solid separating dispenser of embodiment one,
Fig. 3 is the A-A cutaway view of Fig. 2,
Fig. 4 is the B-B cutaway view of Fig. 2,
Fig. 5 is the structural representation of the liquid-solid separating dispenser of embodiment two,
Fig. 6 is the C-C profile of Fig. 5,
Among the figure: 1. the heat pipe that spirals, 2. liquid-solid separating dispenser, 3. feed pump, 4. water tank, 5. fluid inlet tubes, 6. clear water output pipe, 7. liquid-solid separating dispenser, 8. particle control valve, 9. fluid-mixing outlet, 10. clear water exit port pipe, 11. baffles, 12. blow-off pipes.
The specific embodiment:
Embodiment one: a kind of automatic desludging antiscale direct current cooker, by feed pump (3), heat pipe (1) spirals, burner and water controller are formed, installing one cover liquid-solid separating dispenser (2) between the water inlet of the heat pipe that spirals (1) of direct current cooker and venthole, this liquid-solid separating dispenser (2) is made of separate and subside chamber and diversion chamber, top, separate and subside chamber is hollow cylinder, the bottom is a hollow cone, on, be connected between the bottom, clear water output pipe (10) is housed at the top of separate and subside chamber, clear water output pipe (10) is connected with the boiler gas outlet, fluid inlet tubes (5) is housed on the top of separate and subside chamber, fluid inlet tubes (5) is connected with the heat pipe that spirals (1) gas outlet, particle control valve (8) is housed in the bottom of separate and subside chamber, diversion chamber is a hollow cylinder body structure, its inside is provided with the baffle of a band tapering, at the top of diversion chamber the particle inlet tube is housed, the particle inlet tube is connected with particle control valve (8) outlet of bottom, separate and subside chamber, at other clear water inlet tube (10) and the fluid-mixing outlet (9) of also being equipped with respectively of the side of diversion chamber, clear water inlet tube (10) is connected with feed pump (3) outlet, fluid-mixing outlet (9) is connected with the heat pipe that spirals (1) water inlet, blow-off pipe (12) is housed in the bottom of diversion chamber, and blow-off pipe (12) is connected with a stop valve.
Embodiment two: with embodiment one, be the internal structure such as the figure five of liquid-solid separating dispenser with embodiment one difference.
Claims (1)
1. automatic desludging antiscale direct current cooker, by feed pump, heat pipe spirals, burner and water controller are formed, it is characterized in that: the liquid-solid separating dispenser of installing one cover between the water inlet of the heat pipe that spirals of direct current cooker and venthole, this liquid-solid separating dispenser is made of separate and subside chamber and diversion chamber, top, separate and subside chamber is hollow cylinder, the bottom is a hollow cone, on, be connected between the bottom, at the top of separate and subside chamber the clear water output pipe is housed, the clear water output pipe is connected with the boiler gas outlet, fluid inlet tubes is equipped with on top in the separate and subside chamber, fluid inlet tubes is connected with the heat pipe gas outlet of spiraling, in the bottom of separate and subside chamber the particle control valve is housed, diversion chamber is a hollow cylinder body structure, its inside is provided with the baffle of a band tapering, at the top of diversion chamber the particle inlet tube is housed, the particle inlet tube is connected with the particle control valve outlet of bottom, separate and subside chamber, at other clear water inlet tube and the fluid-mixing outlet of also being equipped with respectively of the side of diversion chamber, the clear water inlet tube is connected with the feed pump outlet, the fluid-mixing outlet is connected with the heat pipe water inlet that spirals, blow-off pipe is equipped with in bottom in diversion chamber, and blow-off pipe is connected with a stop valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03248503 CN2651596Y (en) | 2003-08-09 | 2003-08-09 | Automatic descaling and antiscaling DC boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03248503 CN2651596Y (en) | 2003-08-09 | 2003-08-09 | Automatic descaling and antiscaling DC boiler |
Publications (1)
Publication Number | Publication Date |
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CN2651596Y true CN2651596Y (en) | 2004-10-27 |
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ID=34327313
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 03248503 Expired - Fee Related CN2651596Y (en) | 2003-08-09 | 2003-08-09 | Automatic descaling and antiscaling DC boiler |
Country Status (1)
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CN (1) | CN2651596Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106989507A (en) * | 2017-05-19 | 2017-07-28 | 天津市龙津科技有限公司 | Liquid electromagnetic heating boiler system and its control method |
-
2003
- 2003-08-09 CN CN 03248503 patent/CN2651596Y/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106989507A (en) * | 2017-05-19 | 2017-07-28 | 天津市龙津科技有限公司 | Liquid electromagnetic heating boiler system and its control method |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |