CN205957137U - Steam boiler blowdown heat reclamation device - Google Patents
Steam boiler blowdown heat reclamation device Download PDFInfo
- Publication number
- CN205957137U CN205957137U CN201620970191.9U CN201620970191U CN205957137U CN 205957137 U CN205957137 U CN 205957137U CN 201620970191 U CN201620970191 U CN 201620970191U CN 205957137 U CN205957137 U CN 205957137U
- Authority
- CN
- China
- Prior art keywords
- water
- ring
- steam
- boiler
- water inlet
- 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.)
- Expired - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 238000011084 recovery Methods 0.000 claims abstract description 30
- 239000002918 waste heat Substances 0.000 claims abstract description 30
- 238000000926 separation method Methods 0.000 claims description 9
- 238000002955 isolation Methods 0.000 claims description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 5
- 241000893018 Armeria Species 0.000 abstract 1
- 239000000498 cooling water Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 238000007701 flash-distillation Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 208000008425 Protein Deficiency Diseases 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000006392 deoxygenation reaction Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
Abstract
The utility model provides a be used for the boiler waste water of heat supply network and the recovery unit of waste heat, it comprises the column jar body, atomizer, breakwater, buffer, water pump, be equipped with gas vent, cooling water inlet, the import of boiler waste water, delivery port, drain on the column jar body, atomizer establishes on column jar body upper portion, and buffer establishes at column jar body middle part, and the breakwater is established between atomizer and buffer, and the water pump is connected with the delivery port of the column jar body. Its effect lies in: 1, practice thrift the water and the energy, improved the economic benefits of enterprise, 2, can not produce the thermal pollution to the environment, protect the environment.
Description
Technical field：This utility model is related to a kind of auxiliary equipment of steam boiler, and its alternative steam boiler is supporting
Surely the function of row's flash vessel and platoon flash vessel, and most of heat recovery of externally discharge in traditional blowdown flow process is used for carrying
High boiler replenishing water temperature；Particularly a kind of be applied in, the steam boiler blowdown heat reclamation device of low-pressure industrial steam boiler.
Background technology：The process structure of existing steam boiler and auxiliary equipment is shown in accompanying drawing 1, and it is mainly by boiler 1, company
Row's flash vessel 2, surely row's flash vessel 3, steam distributor 4, oxygen-eliminating device 5, softening water tank 6 are pressed and are connected shown in figure.This kind connects
The deficiency that steam boiler and auxiliary equipment exist in use is that waste heat recovery effect is poor, most of heat losses.It
Waste heat recovery is only to enter platoon flash vessel dilatation flash distillation in platoon stove water, and the indirect steam of generation enters oxygen-eliminating device and is used for deoxygenation
This partial heat of heating is recycled, and after dilatation flash distillation, the general temperature of remaining water is (different at 104～160 DEG C about
The different temperature of oxygen-eliminating device operating pressure correspondence), this part water enters after surely arranging flash vessel and directly discharges；The periodical blowdown of boiler
Stove water be also be directly discharged into determine row's flash vessel after directly discharge, all do not recycle, this cause environmental thermal pollution and the energy wave
Take.
Content of the invention：This utility model purpose is, exists in waste heat recovery for existing low-pressure industrial steam boiler
Deficiency, and a kind of steam boiler blowdown heat reclamation device is proposed, it has the advantages that waste heat recovery rate is high.
By following technical proposals, achievable the purpose of this utility model, a kind of steam boiler blowdown heat reclamation device, its
It is characterised by, including waste heat recovery tank, heat exchanger, support；Waste heat recovery tank includes tank body, ring-shape open formula chuck, soda pop are divided
From setting, isolation ring, hydroecium, shower nozzle；The top of tank body is provided with evacuation port, and bottom is provided with hot water outlet, and side wall is respectively equipped with pot
Fire grate wastewater inlet, softening water inlet, boiler blow-off water out；Ring-shape open formula chuck is opening up be located at interior in the middle part of tank body
Wall, steam-water separation equipment is set in ring-shape open formula chuck, and isolation ring is located at the overthe openings of ring-shape open formula chuck, and hydroecium sets
On the top of tank inner chamber, shower nozzle is located at hydroecium bottom, and hydroecium passes through pipeline and is connected with softening water inlet, and boiler blowdown water enters
Mouth and boiler blow-off water out and ring-shape open formula chuck cavity UNICOM；Waste heat recovery tank and heat exchanger are fixed by support；Change
Hot device is provided with room temperature softened water inlet and outlet, and room temperature softens the softening water inlet that water out passes through pipeline and waste heat recovery tank
Connect；Heat exchanger is provided with boiler blow-off water inlet, and it is connected with waste heat recovery tank boiler blow-off water out by pipeline.
Described steam-water separation setting is mainly made up of resistance vapor baffle and packing layer, and resistance vapor baffle is annular flap, and two pieces are
One group of two-way middle part being located at ring-shape open formula chuck, packing layer is located at the top of ring-shape open formula chuck.
For ease of installation and maintenance, waste heat recovery tank is made up of through bolt connection upper cover, canister, low head three.
Effect of the present utility model is：1st, waste heat recovery effect is good, saves the energy, the blowdown of recyclable steam boiler institute
Most heats in water, with existing apparatus ratio, can improve waste heat recovery rate 85～90, this essentially consists in, this device sets
There are two waste-heat recovery devices, the softened water after atomization and the direct condensation by mixing of flash steam guarantee to dodge in waste heat recovery tank
Steam recycles completely；In addition, after flash distillation dilatation in room temperature softened water and the waste heat recovery tank in indirect type heat exchanger
Discharge 95 DEG C of stove water and carry out heat exchange recovery, finally, sewage temperature can be made to drop to less than 40 DEG C and discharge, not only again elimination emitted energy-conservation
Vapour；2nd, simplify device, this is, this device instead of the platoon flash vessel in existing apparatus and surely arranges flash vessel, and, effect
Fruit is also good than both；3rd, it is beneficial to environmental conservation, eliminate the thermal pollution to environment.
Brief description：
The process structure schematic diagram that accompanying drawing 1 is connected with auxiliary equipment for existing steam boiler.
Accompanying drawing 2 is structural representation of the present utility model.
The process structure schematic diagram that accompanying drawing 3 is connected with this utility model and part auxiliary equipment for steam boiler.
Below in conjunction with the accompanying drawings and embodiment is expanded on further to this utility model：
Specific embodiment：
Referring to accompanying drawing 2,3, a kind of steam boiler blowdown heat reclamation device, it mainly by waste heat recovery tank A, heat exchanger B,
Frame C forms.Waste heat recovery tank A mainly by tank body 7, ring-shape open formula chuck 8, steam-water separation setting 9, isolation ring 10, hydroecium 11,
Shower nozzle 12 forms.The top of tank body 7 is provided with evacuation port 13, and bottom is provided with hot water outlet 14, and side wall is respectively equipped with boiler blowdown water
Import 15, softening water inlet 16, boiler blow-off water out 17.Ring-shape open formula chuck 8 is opening up to be located in tank body 7 middle part
Wall, steam-water separation setting 9 is located in ring-shape open formula chuck 8, and its function is that 1 grate furnace water of boiler is carried out steam-water separation.
Isolation ring 10 is located at the overthe openings of ring-shape open formula chuck 8, and its function is not allow the sprayed softened water of shower nozzle 12 enter into ring
Cause in the open chuck of shape 8 to soften water loss.Hydroecium 11 is located at the top of tank body 7 inner chamber, and its function is to make softened water equal
Even be distributed in each shower nozzle, shower nozzle 12 is located at hydroecium 11 bottom.Hydroecium 11 passes through pipeline and is connected with softening water inlet 16.Boiler is arranged
Wastewater inlet 15 is connected with ring-shape open formula chuck 8 cavity with boiler blow-off water out 17.Waste heat recovery tank A and heat exchanger B leads to
Cross support C to fix.Heat exchanger B is provided with room temperature and softens water inlet 18 and soften water out 19, softens water out 19 and passes through pipeline
It is connected with the softening water inlet 16 of waste heat recovery tank.Heat exchanger B is provided with boiler blow-off water inlet 20, and it passes through pipeline and waste heat
Recycling can boiler blow-off water out 17 connects, and heat exchanger B is provided with boiler blow-off water out 21.The setting of described steam-water separation can be by
Resistance vapor baffle 91 and packing layer 92 are constituted, and resistance vapor baffle 91 is annular flap, and two pieces is that one group of two-way ring-shape open formula that is located at is pressed from both sides
The middle part of set 2, packing layer 92 is located at the top of ring-shape open formula chuck 2, and filler is web material.For ease of installation and maintenance,
Tank body 1 is made up of through bolt connection upper cover 71, canister 72, low head 73 three.The platoon outlet of sewer of boiler 1 and fixed row expand
Outlet of sewer is connected with the boiler blow-off water inlet 15 of waste heat recovery tank A by pipeline.The hot water outlet 14 of waste heat recovery tank A leads to
Piping is connected with softening water tank 6.The room temperature of heat exchanger B is softened water inlet 18 and is connected with softening water tank 6 by pipeline.Steam divides
Orchestration 4 one end is connected the other end with boiler 1 and is connected with oxygen-eliminating device 5, oxygen-eliminating device 5 respectively with softening water tank 6, oxygen-eliminating device 5, boiler 1
Connect, softening water tank 6 is connected with oxygen-eliminating device 5, waste heat recovery tank A, heat exchanger B respectively.
The work flow of this device is：The sewage of the continuous blowdown of boiler 1 and periodical blowdown passes through the pot of waste heat recovery tank A
Fire grate wastewater inlet 15 enters and produces vaporization flash distillation in ring-shape open formula chuck 8, and flash-off steam is through resistance vapor baffle 91 and filler
During layer 92, entrained drop is substantially cleared, and carries out through isolation ring 10 entrance tank body 7 inner chamber softened water sprayed with shower nozzle 12
Heat exchange；Steam remove under drop and the remaining sewage of flash distillation pass through boiler blow-off water out 17 and boiler blow-off water inlet 20 and enter
Enter heat exchange cooling in heat exchanger B, afterwards cesspool is drained into by boiler blow-off water out 21 to less than 40 DEG C.Room temperature softened water passes through
Water pump softens water inlet 18 from softening water tank 6 pump water by room temperature and enters heat exchanger B, from softening water out 19 and softening water inlet 16
Enter hydroecium 11, after multiple atomizers 12 are atomized with flash steam after tank body 7 inner chamber condensation by mixing becomes hot water, then from heat
Water out 14 enters in softening water tank 6.
Claims (3)
1. a kind of steam boiler blowdown heat reclamation device is it is characterised in that include waste heat recovery tank, heat exchanger, support；Waste heat returns
Closed cans includes tank body, ring-shape open formula chuck, steam-water separation setting, isolation ring, hydroecium, shower nozzle；The top of tank body is provided with emptying
Mouthful, bottom is provided with hot water outlet, and side wall is respectively equipped with boiler blow-off water inlet, softens water inlet, boiler blow-off water out；Annular
Open chuck is opening up to be located at inwall in the middle part of tank body, and steam-water separation equipment is set in ring-shape open formula chuck, and isolation ring sets
In the overthe openings of ring-shape open formula chuck, hydroecium is located at the top of tank inner chamber, and shower nozzle is located at hydroecium bottom, and hydroecium passes through pipe
Road is connected with softening water inlet, boiler blow-off water inlet and boiler blow-off water out and ring-shape open formula chuck cavity UNICOM；Remaining
Recuperation of heat tank and heat exchanger are fixed by support；Heat exchanger is provided with room temperature softened water inlet and outlet, and room temperature softens water out
It is connected with the softening water inlet of waste heat recovery tank by pipeline；Heat exchanger is provided with boiler blow-off water inlet, it pass through pipeline with
Waste heat recovery tank boiler blow-off water out connects.
2. the steam boiler blowdown heat reclamation device as described in claim 1 is it is characterised in that the setting of described steam-water separation is main
It is made up of resistance vapor baffle and packing layer, resistance vapor baffle is annular flap, two pieces is one group of two-way ring-shape open formula chuck of being located at
Middle part, packing layer is located at the top of ring-shape open formula chuck.
3. the steam boiler blowdown heat reclamation device as described in claim 1 or 2 is it is characterised in that waste heat recovery tank is by upper envelope
Head, canister, low head three form through bolt connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620970191.9U CN205957137U (en) | 2016-08-26 | 2016-08-26 | Steam boiler blowdown heat reclamation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620970191.9U CN205957137U (en) | 2016-08-26 | 2016-08-26 | Steam boiler blowdown heat reclamation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205957137U true CN205957137U (en) | 2017-02-15 |
Family
ID=57981318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620970191.9U Expired - Fee Related CN205957137U (en) | 2016-08-26 | 2016-08-26 | Steam boiler blowdown heat reclamation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205957137U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106338057B (en) * | 2016-08-26 | 2018-08-28 | 盛嘉军 | Steam boiler blowdown heat reclamation device |
-
2016
- 2016-08-26 CN CN201620970191.9U patent/CN205957137U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106338057B (en) * | 2016-08-26 | 2018-08-28 | 盛嘉军 | Steam boiler blowdown heat reclamation device |
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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: 20170215 Termination date: 20190826 |