CN208505057U - A kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation - Google Patents
A kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation Download PDFInfo
- Publication number
- CN208505057U CN208505057U CN201820695279.3U CN201820695279U CN208505057U CN 208505057 U CN208505057 U CN 208505057U CN 201820695279 U CN201820695279 U CN 201820695279U CN 208505057 U CN208505057 U CN 208505057U
- Authority
- CN
- China
- Prior art keywords
- apparatus body
- dissipation
- flushing cinder
- fog
- condensate
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to a kind of condensation fog-dissipation towers for flushing cinder water vapour condensation fog-dissipation, including apparatus body, connecting pipe, exhaust section, steam of flushing cinder import, cooling water inlet, spray spout, condensate canned paragraphs and condensate discharge outlet, exhaust section is arranged on apparatus body top, apparatus body upper inside offers backheat demisting section, condensate canned paragraphs are arranged in apparatus body inner bottom end face, it is provided on the downside of backheat demisting section into vapour condensation segment inside apparatus body, steam of flushing cinder import is connected on the upside of apparatus body right side, apparatus body right side is connected with cooling water inlet, and it is connected with spray spout, connecting pipe is connected on the left of apparatus body, and connecting pipe respectively with being connect into vapour condensation segment and backheat demisting section inside apparatus body, apparatus body inner bottom end face is provided with condensate canned paragraphs, and apparatus body right end Face and condensate canned paragraphs are connected with condensate discharge outlet.
Description
Technical field
The utility model relates to flushing cinder water vapour condensation fog-dissipation apparatus fields, specially a kind of to condense for flushing cinder water vapour
The condensation fog-dissipation tower of fog dispersal.
Background technique
A large amount of high temperature furnace slags are generated after steel plant's blast furnace ironmaking to be cooled down, and are usually all that furnace is carried out using washing slag water
Slag is cooling, and the mode of this cooling of furnace slag is called flush slag.Flush slag carries out blast-furnace slag processing, obtains water after slag water quenching
Slag, grain slag can be made into: portland slag cement, gypsum slag cement, latarge cement, slag brick, slag concrete etc.,
It can be used as a kind of raw material of production environment-protective water adobe.
In the processing method, washing slag water can generate a large amount of water vapour in flushing cinder, and water vapour is arranged by chimney to big
Gas not only wastes a large amount of heat, but also generates a large amount of white hazes, pollutes the environment.State of Blast Furnace is being carried out using flush slag
In the technical process of Slag treatment, the heat of clinker is pulled away in the form of water vapour substantially.Since washing slag water quantity of steam is huge, adopt
With conventional method condensed steam, white haze solution environmental issue is eliminated, investment is very big, is also difficult to solve condensation and fog dispersal simultaneously
The problem of.
The processing that blast-furnace slag is carried out using the INBA method of environmental protection, is directly sprayed water vapour using water, steam is condensed, and is coagulated
Water after knot flows back into flushing cinder pond, then is transported on cooling tower and is cooled down together with the water in flushing cinder pond.This method is due to spray
The water distribution of water drenching is uneven and steam is unevenly distributed, and causes water spray very big, and reddish brown method only condenses
Vapor, there is no eliminate water mist.
Traditional equipment is condensed water vapour using pure air cooling technique, recycles condensed water, because of the water vapour heat that flushing cinder generates
Amount is very big, and the heat transfer coefficient of water vapour and air is small, and the air cooling apparatus for needing to put into is more, and cost is very high, investment and recycling
Cost performance is at a fairly low, does not have practicability, in conclusion being now badly in need of a kind of condensation fog-dissipation for flushing cinder water vapour condensation fog-dissipation
Tower solves the above-mentioned problem.
Utility model content
The utility model aim is to provide a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation, above-mentioned to solve
The traditional equipment proposed in background technique is condensed water vapour using pure air cooling technique, recycles condensed water, because what flushing cinder generated
Water vapour heat is very big, and the heat transfer coefficient of water vapour and air is small, and the air cooling apparatus for needing to put into is more, and cost is very high, throws
Enter with recycling cost performance it is at a fairly low, do not have practicability the problem of.
To achieve the above object, the utility model provides the following technical solutions: one kind being used for flushing cinder water vapour condensation fog-dissipation
Condensation fog-dissipation tower, including apparatus body, connecting pipe, exhaust section, high-efficiency fin heat exchanger tube, steam of flushing cinder import, cooling water
Import, spray spout, hexagon cellular filler, condensate canned paragraphs and condensate discharge outlet, the exhaust section are arranged on apparatus body top
End, the apparatus body upper inside offer backheat demisting section, and the high-efficiency fin heat exchanger tube is located at backheat demisting intersegmental part,
Condensate canned paragraphs setting be provided on the downside of backheat demisting section inside the apparatus body inner bottom end face, the apparatus body into
Vapour condensation segment, the hexagon cellular filler are located at into inside vapour condensation segment, and the spray spout is located inside apparatus body, and position
Between high-efficiency fin heat exchanger tube and hexagon cellular filler, the steam of flushing cinder import is connected on the upside of apparatus body right side,
The apparatus body right side is connected with cooling water inlet, and is connected with spray spout, is connected on the left of the apparatus body
Connecting pipe, and connecting pipe respectively with being connect into vapour condensation segment and backheat demisting section inside apparatus body, the equipment sheet
Internal portion bottom face is provided with condensate canned paragraphs, and apparatus body right side and condensate canned paragraphs are connected with condensate discharge outlet.
Further, the condensate canned paragraphs inner bottom end face is provided with emptying plate.
Further, described to be provided with anti-wall flow ring between vapour condensation segment and backheat demisting section.
Further, high-efficiency fin heat exchanger tube is in tilted layout in the backheat demisting section, inclined direction and steam flowing side
To identical, angle is not less than 15 °.
Further, described to be equipped with packing support into vapour condensation pars infrasegmentalis, top is equipped with filler cover board, and cover board is using porous
Plate, more hollow plate apertures are 10mm.
Further, the anti-wall flow ring is arranged diagonally downward, and tilt angle is 45 °.
Compared with prior art, the utility model has the beneficial effects that the utility model design is a kind of for flushing cinder
The condensation fog-dissipation tower of water vapour condensation fog-dissipation, main purpose are to overcome deficiencies of the prior art and disadvantage, solve
It has determined in the residues processing technique using flush slag, condensing recovery has been carried out to washing slag water steam, while the technology for eliminating white haze is asked
Topic, the present invention not only has considerable water-saving benefit, and solves environmental issue.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
In appended drawing reference: 1. apparatus bodies；2. connecting pipe；3. exhaust section；4. high-efficiency fin heat exchanger tube；5. flushing cinder steams
Vapor inlet；6. cooling water inlet；7. spray spout；8. anti-wall flow ring；9. hexagon cellular filler；10. condensate canned paragraphs；11. solidifying
Water outlet；12. emptying plate.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
All other embodiment obtained, fall within the protection scope of the utility model.
Referring to Fig. 1, the utility model provides a kind of technical solution: a kind of condensation for flushing cinder water vapour condensation fog-dissipation
Disperse fog tower, including apparatus body 1, connecting pipe 2, exhaust section 3, high-efficiency fin heat exchanger tube 4, steam of flushing cinder import 5, cooling water
Import 6, spray spout 7, hexagon cellular filler 9, condensate canned paragraphs 10 and condensate discharge outlet 11, exhaust section 3 are arranged in equipment sheet
1 top of body, 1 upper inside of apparatus body offer backheat demisting section, and high-efficiency fin heat exchanger tube 4 is located at backheat demisting intersegmental part,
The setting of condensate canned paragraphs 10 is provided on the downside of 1 inner bottom end face of apparatus body, 1 inside backheat demisting section of apparatus body into vapour
Condensation segment, hexagon cellular filler 9 are located at into inside vapour condensation segment, and spray spout 7 is located inside apparatus body 1, and are located at efficient
Between fin heat exchange pipe 4 and hexagon cellular filler 9, steam of flushing cinder import 5 is connected on the upside of 1 right side of apparatus body, equipment sheet
1 right side of body is connected with cooling water inlet 6, and is connected with spray spout 7, and connecting pipe 2 is connected on the left of apparatus body 1,
And connecting pipe 2 respectively with being connect into vapour condensation segment and backheat demisting section inside apparatus body 1,1 inner bottom of apparatus body
Face is provided with condensate canned paragraphs 10, and 1 right side of apparatus body and condensate canned paragraphs 10 are connected with condensate discharge outlet 11.
10 inner bottom end face of condensate canned paragraphs, which is provided with, empties plate 12, is provided between vapour condensation segment and backheat demisting section
Anti-wall flow ring 8,4 pipe of high-efficiency fin heat exchanger tube is in tilted layout in backheat demisting section, and inclined direction is identical as steam flow direction, angle
Degree is not less than 15 °, is equipped with packing support into vapour condensation pars infrasegmentalis, top is equipped with filler cover board, and cover board uses porous plate, more hollow plates
Aperture is 10mm, and anti-wall flow ring 8 is arranged diagonally downward, and tilt angle is 45 °.
When the utility model at work: flushing cinder water vapour passes through steam of flushing cinder import 5 first and enters returning for condensation fog-dissipation tower
Hot demisting section, backheat demisting section is using high-efficiency fin pipe as heat exchange original part, and the flushing cinder water vapour of entrance passes through in pipe, through being subcooled
The on-condensible gas for needing to disperse fog after solidifying is outer by pipe, and flushing cinder water vapour transfers heat to the on-condensible gas for needing to disperse fog, and does not coagulate
Gas heating achievees the purpose that aqueous unsaturation to reach demisting, and washing slag water steam cooling reaches washing slag water and tentatively condenses mesh
's.
Flushing cinder water vapour after the cooling of backheat demisting section is entered by pipeline into vapour condensation segment, is used into vapour condensation segment
Hexagon cellular filler 9 can make flushing cinder water vapour and cooling water equal as into vapour distribution original part and cooling water distribution original part, filler
Even contact, to have the function that condense flushing cinder water vapour.
After into the condensation of vapour condensation segment, flushing cinder water vapour has largely all been condensed, the steaming that small part is not condensed
By the ejection umbrella shape water curtain of spray spout 7, water curtain can absorb the vapor not being condensed, while water curtain energy for vapour and non-condensable gas
It is enough to cool down to fixed gas.
Enter backheat demisting section by the fixed gas that spray section again cools down, passes through the high-efficiency fin heat exchanger tube of backheat demisting section
4 exchange heat with the steam of flushing cinder for having just enter into equipment, and playing the role of backheat raising temperature makes itself to reach water content unsaturation
State reaches fog dispersal purpose, while reducing steam of flushing cinder temperature.
Fixed gas after the heating fog dispersal of backheat demisting section is discharged by connecting pipe 2 into exhaust section 3.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above, for
For those skilled in the art, it is clear that the present invention is not limited to the details of the above exemplary embodiments, and without departing substantially from this
In the case where the spirit or essential attributes of utility model, the utility model can be realized in other specific forms.Therefore, no matter
From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the utility model is by institute
Attached claim rather than above description limit, it is intended that will fall within the meaning and scope of the equivalent elements of the claims
All changes are embraced therein.It should not treat any reference in the claims as limiting related right
It is required that.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (6)
1. a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation, it is characterised in that: including apparatus body (1), connection
Pipeline (2), exhaust section (3), high-efficiency fin heat exchanger tube (4), steam of flushing cinder import (5), cooling water inlet (6), spray spout
(7), hexagon cellular filler (9), condensate canned paragraphs (10) and condensate discharge outlet (11), the exhaust section (3) are arranged in equipment sheet
Body (1) top, apparatus body (1) upper inside offer backheat demisting section, and the high-efficiency fin heat exchanger tube (4) is located at back
Hot demisting intersegmental part, condensate canned paragraphs (10) setting is in apparatus body (1) inner bottom end face, the apparatus body (1)
It is provided on the downside of portion's backheat demisting section into vapour condensation segment, the hexagon cellular filler (9) is located at into inside vapour condensation segment, the spray
It sprays mouth (7) and is located at apparatus body (1) inside, and between high-efficiency fin heat exchanger tube (4) and hexagon cellular filler (9), institute
It states steam of flushing cinder import (5) to be connected on the upside of apparatus body (1) right side, apparatus body (1) right side is connected with cooling
Water inlet (6), and be connected with spray spout (7), it is connected with connecting pipe (2) on the left of the apparatus body (1), and communicating pipe
Road (2) respectively with apparatus body (1) is internal connecting into vapour condensation segment and backheat demisting section, apparatus body (1) inner bottom
End face is provided with condensate canned paragraphs (10), and apparatus body (1) right side and condensate canned paragraphs (10) are connected with condensate discharge outlet
(11)。
2. a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation according to claim 1, it is characterised in that: institute
It states condensate canned paragraphs (10) inner bottom end face and is provided with emptying plate (12).
3. a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation according to claim 1, it is characterised in that: institute
It states into being provided with anti-wall flow ring (8) between vapour condensation segment and backheat demisting section.
4. a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation according to claim 1, it is characterised in that: institute
It states high-efficiency fin heat exchanger tube (4) in backheat demisting section to be in tilted layout, inclined direction is identical as steam flow direction, and angle is not less than
15°。
5. a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation according to claim 1, it is characterised in that: institute
It states into vapour condensation pars infrasegmentalis and is equipped with packing support, top is equipped with filler cover board, and cover board uses porous plate, and more hollow plate apertures are
10mm。
6. a kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation according to claim 3, it is characterised in that: institute
It states anti-wall flow ring (8) to arrange diagonally downward, tilt angle is 45 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820695279.3U CN208505057U (en) | 2018-05-09 | 2018-05-09 | A kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820695279.3U CN208505057U (en) | 2018-05-09 | 2018-05-09 | A kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208505057U true CN208505057U (en) | 2019-02-15 |
Family
ID=65298276
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820695279.3U Active CN208505057U (en) | 2018-05-09 | 2018-05-09 | A kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208505057U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109881738A (en) * | 2019-04-26 | 2019-06-14 | 秦皇岛莱特流体设备制造有限公司 | A kind of washing slag water steam exhaust fog dissipation system and defogging method |
| CN110093465A (en) * | 2019-04-16 | 2019-08-06 | 浙江菲达环保科技股份有限公司 | A kind of blast furnace slag flushing vapor disappears white system and method |
-
2018
- 2018-05-09 CN CN201820695279.3U patent/CN208505057U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110093465A (en) * | 2019-04-16 | 2019-08-06 | 浙江菲达环保科技股份有限公司 | A kind of blast furnace slag flushing vapor disappears white system and method |
| CN110093465B (en) * | 2019-04-16 | 2021-06-08 | 浙江菲达环保科技股份有限公司 | Blast furnace slag flushing steam whitening system and method |
| CN109881738A (en) * | 2019-04-26 | 2019-06-14 | 秦皇岛莱特流体设备制造有限公司 | A kind of washing slag water steam exhaust fog dissipation system and defogging method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108465368A (en) | Desulfurization and dedusting disappears white device for deep cleaning | |
| CN107120714A (en) | A kind of thermal power plant boiler fume afterheat is used for the whole yearization comprehensive utilization energy conserving system of central heating or heating boiler feed water | |
| CN208678740U (en) | Waste gas produced device when a kind of processing melting waste aluminum | |
| CN208505057U (en) | A kind of condensation fog-dissipation tower for flushing cinder water vapour condensation fog-dissipation | |
| CN207648831U (en) | A kind of efficiently water intaking eliminating white smoke cooperation-removal pollutant device | |
| CN109974062A (en) | A kind of fume afterheat depth recovery system using absorption heat pump and two-stage heat exchanger | |
| CN206935061U (en) | A kind of wet desulfurization flue gas processing unit | |
| CN104087691B (en) | The technique of washing slag water steam heat recovery and fog dispersal and the equipment adopted | |
| CN106191345B (en) | A kind of converter melts red slag heat recovering device and exhaust heat recovering method | |
| CN207648835U (en) | A kind of boiler exhaust gas waste heat recovery heat supply three towers unification heat transfer spray tower | |
| CN203976821U (en) | A kind of equipment for the waste heat recovery of flushing cinder water vapor and fog dispersal | |
| CN208632574U (en) | A kind of blast furnace slag quenching water disappears white device | |
| CN106636496B (en) | A kind of Dry granulation of BF slag and heat recovery system and method | |
| CN208493801U (en) | A kind of desulfurization and dedusting disappears white device for deep cleaning | |
| CN208090710U (en) | A kind of tubular type condensation heat exchange system of achievable dropwise condensation | |
| CN208395214U (en) | A kind of blast furnace slag flushing steam disappears white system | |
| CN206832073U (en) | A kind of steam cooling recovery system | |
| CN213596310U (en) | Blast furnace quenching slag steam preheating air system | |
| CN110129493A (en) | A kind of recycling of blast furnace water slag-flushing process waste and steam disappear white system and method | |
| CN109589639A (en) | A kind of steel blast furnace slag flushing steam white cigarette elimination system | |
| CN109925870A (en) | A kind of low-temperature flue gas of wet desulphurization disappears white system | |
| CN214168013U (en) | Environment-friendly blast furnace slag treatment steam recovery system | |
| CN210206387U (en) | Self-heating flue gas white eliminating device | |
| CN208933401U (en) | A kind of system that blast furnace slag flushing water system eliminates " white cigarette " | |
| CN209292377U (en) | A kind of blast furnace granulated slag energy saving technology disappears white processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |