CN204043191U - A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler - Google Patents
A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler Download PDFInfo
- Publication number
- CN204043191U CN204043191U CN201420433851.0U CN201420433851U CN204043191U CN 204043191 U CN204043191 U CN 204043191U CN 201420433851 U CN201420433851 U CN 201420433851U CN 204043191 U CN204043191 U CN 204043191U
- Authority
- CN
- China
- Prior art keywords
- water
- boiler
- wall
- denitration
- traveling
- 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.)
- Withdrawn - After Issue
Links
Abstract
The utility model relates to a kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler, comprise boiler furnace and traveling-grate stoker part, wherein, traveling-grate stoker part is arranged on the bottom of boiler furnace part, it is characterized in that: a boiler water cycle mechanism is set on boiler body, it is by passage rear wall water-cooling wall and expansion chamber upper collecting chamber, lower header forms, boiler body arranges spray denitration cyclonic separation sedimentation device, it is by denitration shower, denitration nozzle, denitrfying agent feeder, upper sedimentation separation room, lower sedimentation separation chamber composition, there is solution heating surface area little, furnace outlet flue gas does not directly wash away Flag pattern heat surface coiled pipe, reduce wear, prolonged boiler service life, reduce the discharge that maintenance frequency reduces nitrogen oxide, reduce air pollution, improve the thermal efficiency, the features such as energy-saving environmental protection safety.
Description
technical field
The utility model relates to boiler technology field, particularly can meet the emission request of national emission standard of air pollutants for boilers, solves discharged nitrous oxides concentration high, a kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler of contaminated environment.
background technology
As everyone knows, current corner tube boiler structure arranges around boiler body that four down-comers be not heated are as support.Furnace outlet flue gas directly washes away Flag pattern heat surface coiled pipe, and serious wear does not have expansion chamber, and dust can not sedimentation, and heating surface is few, and service life is low, and maintenance rate is high, increases use cost.Along with national environmental protection policy is increasingly strict, known corner tube boiler can not meet the emission request of country about emission standard of air pollutants for boilers, and discharged nitrous oxides concentration is high, contaminated environment.Therefore, how to solve boiler and do not have expansion chamber and ash fall, and it is little to solve heating surface area, furnace outlet flue gas does not directly wash away Flag pattern heat surface coiled pipe, reduce wear, prolonged boiler service life, reduce maintenance frequency, reduce use cost, in addition, solve Denitration in Boiler, reduce discharged nitrous oxides, energy-conserving and environment-protective etc. have become problem in the urgent need to address at present.
summary of the invention
The purpose of this utility model is: improve for the ubiquitous problem of prior art, overcome shortcomings and deficiencies of the prior art, there is provided a kind of with expansion chamber, reduce the discharge of nitrogen oxide, improve the single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler of boiler thermal output.
The utility model solves the technical scheme that its technical problem adopts: a kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler, comprise boiler furnace part, traveling-grate stoker part, boiler furnace part comprises boiler body 1, four of the setting of boiler body 1 surrounding vertical have side wall down-comer 5 and the rear arch feed pipe 27 of supporting role, at the drum 3 that boiler body 1 upper left is arranged, the water inlet pipe 2 be communicated with drum 3, Flag pattern heat surface feed pipe 14, face arch down-comer 4, and down-comer 26 and last time water pipe 15, side water wall 6, burner hearth 7, face arch water-cooling wall 8, face arch lower header 9, side wall lower header 10, side water wall upper collecting chamber 16, front and back arch upper collecting chamber 17, outlet pipe 19, Flag pattern heat surface upper collecting chamber 20
,flag pattern heat surface pipe 22, exhanst gas outlet 23, Flag pattern heat surface 25, rear arch water-cooling wall 31, Flag pattern heat surface lower header 32, lower header 33, and dust export 34, traveling-grate stoker part is arranged on the bottom of boiler furnace part and is connected with the boiler body 1 of boiler furnace part, it is characterized in that:
A, rear arch water-cooling wall 31 at the boiler body 1 of boiler furnace part, arrange a boiler water cycle mechanism between Flag pattern heat surface 25 and side water wall 6, it is by passage rear wall water-cooling wall 30 and expansion chamber upper collecting chamber 18, and lower header 33 forms, as Figure 1-5.
B, at the rear arch water-cooling wall 31 of the boiler body 1 of boiler furnace part, spray denitration cyclonic separation sedimentation device is set between the passage rear wall water-cooling wall 30 of boiler water cycle mechanism and side water wall 6, it is by denitration shower 28, denitration nozzle 24, denitrfying agent feeder 35, upper sedimentation separation room 21, lower sedimentation separation chamber 29 forms, wherein, uniform passage rear wall water-cooling wall 30 upper interval being horizontally set on rear arch water-cooling wall 31 and boiler water cycle mechanism of denitration shower 28, uniform on denitration shower 28 denitration nozzle 24 is set, realize unidirectional spray denitration sedimentation separation, the bottom of denitration shower 28 is communicated with denitrfying agent feeder 35, as Fig. 1, 2, shown in 5.Here, denitration nozzle 24 also uniformly can arrange denitration nozzle 24 denitration shower 28 is upper and lower, realizes Bidirectional spray denitration sedimentation separation, as shown in Figure 3,4.In addition, denitration shower 28 can be designed as many rows up and down, such as two rows, or three or four rows.
C, traveling-grate stoker partial design adopt traveling-grate stoker structure, and it is by traveling-grate stoker 11, slip expanding stent 12, and boiler supports 13 forms, as Figure 1-5.
The passage rear wall water-cooling wall 30 of said boiler water cycle mechanism is designed to the top indent of co-current contact after the first adverse current of cyclone type, lower lobes inverted S-shaped, further, passage rear wall water-cooling wall 30 is upper and lower to be communicated with lower header 33 with expansion chamber upper collecting chamber 18 respectively, as Figure 1-5.
The upper sedimentation separation room 21 of said spray denitration cyclonic separation sedimentation device is by rear arch water-cooling wall 31, passage rear wall water-cooling wall 30, side water wall 6, and denitration nozzle 24 and denitration shower 28 upper part interval form, lower sedimentation separation chamber 29 is formed by between passage rear wall water-cooling wall 30 bottom and Flag pattern heat surface 25 lower region, as Figure 1-5.
The course of work and the principle of this technology are: be first, coal is fallen on traveling-grate stoker 11 under gravity, send under machine power effect in burner hearth 7 and burn, produce heat by the face arch water-cooling wall 8 of burner hearth, rear arch water-cooling wall 31, side water wall 6 absorbs, flue gas after cooling behind upper sedimentation separation room 21 on be advanced into that separation chamber 29 falls in sinking, Flag pattern heat surface 25 carries out washing away heat exchange, complete whole heat transfer process, afterwards, discharged by exhanst gas outlet 23.Here, dust is discharged by dust export 34 after lower sedimentation separation chamber 29 sedimentation, completes the boiler smoke course of work.Next is that boiler water cycle process is that boiler blow-down water flows into drum 3 through water inlet pipe 2, and boiler water outlet is flowed out through outlet pipe 19.Concrete one is fed water by drum 3, face arch down-comer 4, face arch lower header 9, arch upper collecting chamber 17 before and after flowing into after traveling-grate stoker 11 and burner hearth 7 heat exchange, last time water pipe 15 get back to drum 3, complete face arch water-cooling wall 8 water circulation; Two is by drum 3, and side wall down-comer 5, side wall lower header 10 feed water, after traveling-grate stoker 11 and burner hearth 7 heat exchange, flow into side water wall upper collecting chamber 16, and last time, water pipe 15 got back to drum 3, completed side water wall 6 water circulation; Three is by drum 3, rear arch feed pipe 27, down-comer 26, lower header 33 feed water, arch upper collecting chamber 17 before and after flowing into after traveling-grate stoker 11 and burner hearth 7 heat exchange, expansion chamber upper collecting chamber 18, last time water pipe 15 get back to drum 3, complete rear arch water-cooling wall 31, passage rear wall water-cooling wall 30 water circulation; Four is fed water by drum 3, Flag pattern heat surface feed pipe 14, enters Flag pattern heat surface lower header 32, Flag pattern heat surface pipe 22, Flag pattern heat surface 25, Flag pattern heat surface upper collecting chamber 20, completes Flag pattern heat surface 25 water circulation, by outlet pipe 19 water outlet, complete the whole course of work.What needs stressed is this technology spray denitration cyclonic separation sedimentation device and boiler water cycle mechanism, the former mainly carries out spray denitration and cyclonic separation sedimentation, after the first adverse current of the denitrfying agent that exiting flue gas and the denitration nozzle 24 of burner hearth 7 eject, following current contacts, in denitration Sproy cyclone separate and subside room 21, namely go up in separate and subside room 21 and lower sedimentation separation chamber 29 and carry out chemical reaction, complete denitrating flue gas depositing dust separate and subside process, reduce discharged nitrous oxides, energy-conserving and environment-protective, this technology spray denitration cyclonic separation sedimentation device can be widely used on other various boiler.The latter mainly carries out adding one group of boiler water cycle process, namely passage rear wall water-cooling wall 30 is designed to the top indent of co-current contact after the first adverse current of cyclone type, inverted S-shaped (or being called arc cyclone structure) of lower lobes, improve heating surface area little, furnace outlet flue gas does not directly wash away Flag pattern heat surface coiled pipe, reduce wear, prolonged boiler service life, reduce maintenance frequency, reduce use cost, in addition, this technology is not limited only to the structure of traveling-grate stoker 11, also other fire grate structure can be adopted, such as reciprocal grate structure etc.In this technology, denitrfying agent adopts liquefied ammonia, ammonia, urea liquid.A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler of this technology is hot-water boiler, steam boiler etc., also can be the boiler of other type.In addition, this technology can be widely used in other various corner tube boiler.
The beneficial effect of this technology is compared had feature with existing technology in other words and is: design spray denitration cyclonic separation sedimentation device and boiler water cycle mechanism, be provided with the sedimentation separation room of spray denitration and cyclone separating structure, there is heating surface area large, furnace outlet flue gas does not directly wash away Flag pattern heat surface coiled pipe, reduce wear, prolonged boiler service life, reduce maintenance frequency, reduce use cost, reduce the discharge of nitrogen oxide, reduce air and contamination by dust, improve boiler thermal output, the features such as energy-saving environmental protection safety.
Accompanying drawing explanation
Fig. 1 is the front view of the utility model (spray denitration pipe 28 top arranges denitration nozzle 24, and passage rear wall water-cooling wall 30 is top indent, lower lobes inverted S-shaped).
Fig. 2 is that (spray denitration pipe 28 top arranges denitration nozzle 24 to the utility model the second structure, passage rear wall water-cooling wall 30 is vertically disposed upper part two passage rear wall water-cooling walls 30, and lower part merges and is communicated with is the structure of a passage rear wall water-cooling wall 30) front view.
Fig. 3 is the front view of the third structure of the utility model (spray denitration pipe 28 is upper and lower arranges denitration nozzle 24, and passage rear wall water-cooling wall 30 is for being top indent, the inverted S-shaped structure of lower lobes).
Fig. 4 is that (spray denitration pipe 28 is upper and lower arranges denitration nozzle 24 to the utility model the 4th kind of structure, passage rear wall water-cooling wall 30 is vertically disposed upper part two passage rear wall water-cooling walls 30, and lower part merges and is communicated with is the structure of a passage rear wall water-cooling wall 30) front view.
Fig. 5 is that (spray denitration pipe 28 top arranges denitration nozzle 24 to the utility model the 5th kind of structure, passage rear wall water-cooling wall 30 is top indent, the inverted S-shaped structure of lower lobes, and 19 outlet pipes are arranged on below, note: above four kinds be all arrange superincumbent) front view.
In figure: 1 boiler body, 2 water inlet pipes, 3 drums, 4 face arch down-comers, 5 side wall down-comers (or being called port side boiler support-side water-cooling wall down-comer), 6 side water walls, 7 burner hearths, 8 face arch water-cooling walls, 9 face arch lower headers, 10 side wall lower headers, 11 traveling-grate stokers, 12 slip expanding stents, 13 boiler supports, 14 Flag pattern heat surface feed pipes, 15 last time water pipe, 16 side water wall upper collecting chambers, encircle upper collecting chamber before and after 17,18 expansion chamber upper collecting chambers, 19 outlet pipes, 20 Flag pattern heat surface upper collecting chambers
,sedimentation separation room (or being called spray denitration cyclone settling separation chamber) on 21, 22 Flag pattern heat surface pipes, 23 exhanst gas outlets, 24 denitration nozzle, 25 Flag pattern heat surfaces, 26 down-comers (or being called rear arch passage rear wall down-comer), 27 rear arch feed pipes (or being called that starboard boiler supports rear arch feed pipe), 28 spray denitration pipes, 29 times sedimentation separation chambers (or being called sedimentation separation room), 30 passage rear wall water-cooling walls, 31 rear arch water-cooling walls, 32 Flag pattern heat surface lower headers, 33 lower headers (or being called rear arch water-cooling wall passage rear wall lower header), 34 dust exports, 35 denitrfying agent feeders (or being called denitrfying agent feedway).
detailed description of the invention
Detailed description of the invention of the present utility model, as Figure 1-5, a kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler, comprise boiler furnace part, traveling-grate stoker part, boiler furnace part comprises boiler body 1, four of the setting of boiler body 1 surrounding vertical have side wall down-comer 5 and the rear arch feed pipe 27 of supporting role, at the drum 3 that boiler body 1 upper left is arranged, the water inlet pipe 2 be communicated with drum 3, Flag pattern heat surface feed pipe 14, face arch down-comer 4, and down-comer 26 and last time water pipe 15, side water wall 6, burner hearth 7, face arch water-cooling wall 8, face arch lower header 9, side wall lower header 10, side water wall upper collecting chamber 16, front and back arch upper collecting chamber 17, outlet pipe 19, Flag pattern heat surface upper collecting chamber 20
,flag pattern heat surface pipe 22, exhanst gas outlet 23, Flag pattern heat surface 25, rear arch water-cooling wall 31, Flag pattern heat surface lower header 32, lower header 33, and dust export 34, traveling-grate stoker part is arranged on the bottom of boiler furnace part and is connected with the boiler body 1 of boiler furnace part, it is characterized in that:
A, rear arch water-cooling wall 31 at the boiler body 1 of boiler furnace part, arrange a boiler water cycle mechanism between Flag pattern heat surface 25 and side water wall 6, it is by passage rear wall water-cooling wall 30 and expansion chamber upper collecting chamber 18, and lower header 33 forms, as Figure 1-5.
B, at the rear arch water-cooling wall 31 of the boiler body 1 of boiler furnace part, spray denitration cyclonic separation sedimentation device is set between the passage rear wall water-cooling wall 30 of boiler water cycle mechanism and side water wall 6, it is by denitration shower 28, denitration nozzle 24, denitrfying agent feeder 35, upper sedimentation separation room 21, lower sedimentation separation chamber 29 forms, wherein, uniform passage rear wall water-cooling wall 30 upper interval being horizontally set on rear arch water-cooling wall 31 and boiler water cycle mechanism of denitration shower 28, uniform on denitration shower 28 denitration nozzle 24 is set, realize unidirectional spray denitration sedimentation separation, the bottom of denitration shower 28 is communicated with denitrfying agent feeder 35, as Fig. 1, 2, shown in 5.Here, denitration nozzle 24 also uniformly can arrange denitration nozzle 24 denitration shower 28 is upper and lower, realizes Bidirectional spray denitration sedimentation separation, as shown in Figure 3,4.In addition, denitration shower 28 can be designed as many rows up and down, such as two rows, or three or four rows.
C, traveling-grate stoker partial design adopt traveling-grate stoker structure, and it is by traveling-grate stoker 11, slip expanding stent 12, and boiler supports 13 forms, as Figure 1-5.
The passage rear wall water-cooling wall 30 of said boiler water cycle mechanism is designed to the top indent of co-current contact after the first adverse current of cyclone type, lower lobes inverted S-shaped, further, passage rear wall water-cooling wall 30 is upper and lower to be communicated with lower header 33 with expansion chamber upper collecting chamber 18 respectively, as Figure 1-5.
The upper sedimentation separation room 21 of said spray denitration cyclonic separation sedimentation device is by rear arch water-cooling wall 31, passage rear wall water-cooling wall 30, side water wall 6, and denitration nozzle 24 and denitration shower 28 upper part interval form, lower sedimentation separation chamber 29 is formed by between passage rear wall water-cooling wall 30 bottom and Flag pattern heat surface 25 lower region, as Figure 1-5.
Claims (3)
1. a single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler, comprise boiler furnace part, traveling-grate stoker part, boiler furnace part comprises boiler body (1), four of the setting of boiler body (1) surrounding vertical have side wall down-comer (5) and the rear arch feed pipe (27) of supporting role, at the drum (3) that boiler body (1) upper left is arranged, the water inlet pipe (2) be communicated with drum (3), Flag pattern heat surface feed pipe (14), face arch down-comer (4), and down-comer (26) and water pipe last time (15), side water wall (6), burner hearth (7), face arch water-cooling wall (8), face arch lower header (9), side wall lower header (10), side water wall upper collecting chamber (16), front and back arch upper collecting chamber (17), outlet pipe (19), Flag pattern heat surface upper collecting chamber (20)
,flag pattern heat surface pipe (22), exhanst gas outlet (23), Flag pattern heat surface (25), rear arch water-cooling wall (31), Flag pattern heat surface lower header (32), lower header (33), and dust export (34), traveling-grate stoker part is arranged on the bottom of boiler furnace part and is connected with the boiler body (1) of boiler furnace part, it is characterized in that:
A, rear arch water-cooling wall (31) at the boiler body (1) of boiler furnace part, one boiler water cycle mechanism is set between Flag pattern heat surface (25) and side water wall (6), it is by passage rear wall water-cooling wall (30) and expansion chamber upper collecting chamber (18), and lower header (33) forms;
B, at the rear arch water-cooling wall (31) of the boiler body (1) of boiler furnace part, spray denitration cyclonic separation sedimentation device is set between the passage rear wall water-cooling wall (30) of boiler water cycle mechanism and side water wall (6), it is by denitration shower (28), denitration nozzle (24), denitrfying agent feeder (35), upper sedimentation separation room (21), lower sedimentation separation chamber (29) composition, wherein, uniform passage rear wall water-cooling wall (30) upper interval being horizontally set on rear arch water-cooling wall (31) and boiler water cycle mechanism of denitration shower (28), denitration shower (28) is above uniform arranges denitration nozzle (24), the bottom of denitration shower (28) is communicated with denitrfying agent feeder (35),
C, the design of traveling-grate stoker portion adopt traveling-grate stoker structure, and it is by traveling-grate stoker (11), slip expanding stent (12), and boiler supports (13) forms.
2. a kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler as claimed in claim 1, it is characterized in that: the passage rear wall water-cooling wall (30) of said boiler water cycle mechanism is designed to the top indent of co-current contact after the first adverse current of cyclone type, lower lobes inverted S-shaped, further, passage rear wall water-cooling wall (30) is upper and lower is communicated with lower header (33) with expansion chamber upper collecting chamber (18) respectively.
3. a kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler as claimed in claim 1 or 2, it is characterized in that: the upper sedimentation separation room (21) of said spray denitration cyclonic separation sedimentation device is by rear arch water-cooling wall (31), passage rear wall water-cooling wall (30), side water wall (6), and denitration nozzle (24) and denitration shower (28) upper part interval form, lower sedimentation separation chamber (29) is formed by between passage rear wall water-cooling wall (30) bottom and Flag pattern heat surface (25) lower region.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420433851.0U CN204043191U (en) | 2014-08-04 | 2014-08-04 | A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420433851.0U CN204043191U (en) | 2014-08-04 | 2014-08-04 | A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204043191U true CN204043191U (en) | 2014-12-24 |
Family
ID=52243847
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420433851.0U Withdrawn - After Issue CN204043191U (en) | 2014-08-04 | 2014-08-04 | A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204043191U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105318535A (en) * | 2014-08-04 | 2016-02-10 | 哈尔滨四方锅炉安装有限公司 | Single-boiler-barrel transversely-arranging type chain grate stoker spraying and denitration corner-tube boiler |
| CN109340737A (en) * | 2018-11-19 | 2019-02-15 | 哈尔滨红光锅炉总厂有限责任公司 | A kind of corner tube boiler can be used for SCR denitration |
-
2014
- 2014-08-04 CN CN201420433851.0U patent/CN204043191U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105318535A (en) * | 2014-08-04 | 2016-02-10 | 哈尔滨四方锅炉安装有限公司 | Single-boiler-barrel transversely-arranging type chain grate stoker spraying and denitration corner-tube boiler |
| CN105318535B (en) * | 2014-08-04 | 2018-05-15 | 哈尔滨四方锅炉有限公司 | A kind of single drum horizontal formula traveling-grate stoker sprays denitration corner tube boiler |
| CN109340737A (en) * | 2018-11-19 | 2019-02-15 | 哈尔滨红光锅炉总厂有限责任公司 | A kind of corner tube boiler can be used for SCR denitration |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105318535B (en) | A kind of single drum horizontal formula traveling-grate stoker sprays denitration corner tube boiler | |
| CN105318307A (en) | Two-drum horizontal settling chamber spraying denitration corner-tube boiler | |
| CN205090598U (en) | Coal -fired powder boiler of vertical extreme misery tubular construction | |
| CN201463253U (en) | Double-furnace horizontal type industrial pulverized coal fired boiler | |
| CN101929669A (en) | Vertical industrial pulverized coal boiler system | |
| CN204043191U (en) | A kind of single drum horizontal formula traveling-grate stoker spray denitration corner tube boiler | |
| CN204100568U (en) | A kind of single drum horizontal formula reciprocal grate spray denitration corner tube boiler | |
| CN104613638A (en) | Inner container biomass boiler | |
| CN104406144A (en) | Double-medium waste heat boiler | |
| CN204301027U (en) | Verticle coal-burning stem boiler | |
| CN204026649U (en) | Device for utilizing waste of boiler | |
| CN204062980U (en) | A kind of double-barrel transverse formula expansion chamber spray denitration corner tube boiler | |
| CN204345599U (en) | A kind of spray denitration boiler with expansion chamber | |
| CN105318309A (en) | Two-drum spraying denitration settling separation corner-tube boiler | |
| CN204062978U (en) | A kind of two drum expansion chamber spray denitration corner tube boiler | |
| CN204062982U (en) | A kind of two drum spray denitration sedimentation separation corner tube boiler | |
| CN201837052U (en) | Environment-friendly and energy-saving boiler | |
| CN104595894A (en) | System and method for solving high-sodium coal combustion contamination by low-wall-temperature heat exchange surface | |
| CN104315872B (en) | Boiler flue gas waste heat recycling and energy-saving device with boiler flue gas dust removing effect | |
| CN102798112B (en) | Boiler capable of preventing scorification and dust stratification | |
| CN105318536A (en) | Single-boiler-barrel transversely-arranging type reciprocating grate spraying and denitration corner-tube boiler | |
| CN204630028U (en) | Inner bag biomass boiler | |
| CN104165349B (en) | Device for utilizing waste of boiler | |
| CN204063011U (en) | A kind of fluidized bed semicoke thermal vector system preventing boiler from staiing | |
| CN203478218U (en) | Compact type circulating fluidized bed boiler capable of cleanly combusting high-sodium coal |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141224 Effective date of abandoning: 20180515 |
|
| AV01 | Patent right actively abandoned |