CN206094053U - Energy -conserving economizer of bed coal fired boiler is vulcanized in circulation - Google Patents
Energy -conserving economizer of bed coal fired boiler is vulcanized in circulation Download PDFInfo
- Publication number
- CN206094053U CN206094053U CN201621002520.7U CN201621002520U CN206094053U CN 206094053 U CN206094053 U CN 206094053U CN 201621002520 U CN201621002520 U CN 201621002520U CN 206094053 U CN206094053 U CN 206094053U
- Authority
- CN
- China
- Prior art keywords
- economizer
- membrane
- tubes
- higher level
- subordinate
- 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- Withdrawn - After Issue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 discloses an energy -conserving economizer of bed coal fired boiler is vulcanized in circulation, include from last to connecting down higher level's economizer, SCR catalyst structure and the subordinate's economizer in the boiler, higher level's economizer include from last to higher level's economizer export collection case of setting gradually down, go up membrane type coal economizer pipe and higher level's economizer import collection case, subordinate's economizer includes respectively to the subordinate's economizer export collection case that sets gradually down, membrane type coal economizer pipe and subordinate's economizer import collection case down, higher level's economizer import collection case passes through pipeline no. 1 and connects the water route that subordinate's economizer exported the collection case with pipeline no. 2. The utility model discloses an energy -conserving economizer has reduced boiler nox and has discharged, has reduced environmental pollution, has adapted to present environmental protection requirement, realizes installing SCR denitration catalyst additional to the boiler, improves its production efficiency.
Description
Technical field
This utility model is related to the economizer technical field of 75t/h circulating fluidized bed combustion coal boilers, more particularly to circulates
Vulcanization bed coal-burning boiler energy-saving economizer.
Background technology
Technology of Circulating Fluidized Bed Boiler is the high-efficiency low-pollution cleaning burning branch art for developing rapidly in recent ten years.State
On border, this technology the field such as utilizes to have obtained widespread commercial use in station boiler, Industrial Boiler and offal treatment, and
Develop to the large circulating fluidized bed boiler of hundreds of thousands multikilowatt scale;Domestic research in this respect, development and application also by
Gradually rise, among existing up to a hundred CFBBs put into operation or manufacturing.
Boiler is generally divided into two vertical shafts in front portion and afterbody using single drum, natural circulation mode.Anterior vertical shaft is total
Structure is hung, surrounding is made up of fin panel casing.From bottom to top, air compartment, emulsion zone, a dilute-phase zone are followed successively by, back-end ductwork is certainly
High temperature superheater, low temperature superheater and economizer, air preheater are followed successively by under above.Tail vertical well adopts supporting construction, and two
It is connected by vertical cyclone separator between vertical shaft, separator bottom couples loop back device and ash cooler.Combustor and separation
Abrasionproof liner, anterior vertical shaft tube, external metal casing, tail vertical well light boiler setting, by eight are equipped with inside device
Root steel column bears boiler total weight.
Boiler adopts ignition under bed(Oil or coal gas), fractional combustion, First air ratio account for 50-60%, and flying dust circulation is low
Multiplying power, middle temperature separate lime-ash discharge and adopt dry type, are discharged by water-cooling spiral tapping machine, ash cooler and dust collector ash hopper respectively.
Burner hearth is the key for ensureing full combustion of fuel, using turbulent bed so that fluidizing velocity is in 3.5-4.5m/s, and designs appropriate
Section of burner hearth, lay thin liner on burner hearth membrane wall pipe(High-Alumina brick)Even if, during boiler combustion different fuel, burning
Efficiency is also held in more than 98-99%.
, at 800 DEG C or so, cyclone cylinder internal diameter is less for high-temperature separator inlet flue gas temperature, and structure simplifies, and only needs one layer thin in cylinder
Thin abrasionproof liner(Nitridation silica brick).Its service life is longer.Circulating ratio is 10-20 or so.
Circulating ash induction system is mainly by a few part compositions such as feed back pipe, loop back device, overflow pipe and ash cooler.
The regulation process of bed temperature control system is automatic.Concentrated phase bed bed temperature is remained in the range of whole load variations
A certain steady state value between 850-950 DEG C, this value are optimal desulfurization temperatures.When automatically control do not put into when, armrest is dynamic also
Maintain constant bed temperature.
Environmental protection, energy saving are the problems of every country long-run development overriding concern, and CFBB is exactly
Grown up based on this point, its high reliability, high stability, high availability, optimal environmental protection characteristic and extensive
Fuel tolerance, the particularly adaptability to inferior fuel, increasingly receive significant attention, entirely appropriate China's national situation and development
Advantage.But existing 75t/h circulating fluidized bed combustion coals boiler, boiler have after putting into operation that Nox is discharged, and are not inconsistent
Related environment protection index and requirement are closed, so need to make improvements.
Utility model content
In order to overcome the above-mentioned deficiencies of the prior art, this utility model provides circulating fluid-bed coal-burning boiler energy-saving and saves coal
Device, its object is to, to reduce boiler Nox discharges, reduce environmental pollution, adapts to current environmental requirement, and realization is carried out to boiler
Install the technological transformation of SCR denitration additional.
The technical scheme adopted by this utility model is:Circulating fluid-bed coal-burning boiler energy-saving economizer, including from up to
Under be connected to higher level's economizer in boiler, SCR catalyst structure and subordinate's economizer, higher level's economizer include from top to bottom according to
Higher level's economizer exit header of secondary setting, upper the Tubes of Membrane Economizer and higher level's economizer import header, subordinate's economizer difference
Including the subordinate's economizer exit header, lower the Tubes of Membrane Economizer and subordinate's economizer import header that up to set gradually down;On
Level economizer import header passes through pipeline one and pipeline two connects the water route of subordinate's economizer exit header.
Further, upper the Tubes of Membrane Economizer and lower the Tubes of Membrane Economizer be set up in parallel by some row's membrane wall pipes respectively and
Into the row of the membrane wall pipe of lower the Tubes of Membrane Economizer is more than the row of the membrane wall pipe of upper the Tubes of Membrane Economizer.
Further, the row of the membrane wall pipe of upper the Tubes of Membrane Economizer is-row, the membrane wall pipe of lower the Tubes of Membrane Economizer
Row for-row, and total row of upper the Tubes of Membrane Economizer and lower the Tubes of Membrane Economizer for row.
Further, connected and fixed by some comb plate, comb joints between the membrane wall pipe of upper the Tubes of Membrane Economizer, lower membrane type is saved
Connect and fix also by some comb plate, comb joints between the membrane wall pipe of coal device pipe.
Further, upper the Tubes of Membrane Economizer and lower the Tubes of Membrane Economizer are fixed on boiler furnace by a support respectively
On.
Compared with prior art, the beneficial effects of the utility model are:Circulating fluid-bed coal-burning boiler of the present utility model
Energy-saving coal-saving device, in existing boiler economizer, increased the fore-and-aft distance between higher level's economizer and subordinate's economizer and adds
Hot face, and higher level's economizer include setting gradually from top to bottom higher level's economizer exit header, upper the Tubes of Membrane Economizer and
Higher level's economizer import header, subordinate's economizer include subordinate's economizer exit header, the lower film for up to setting gradually down respectively
Formula economizer tube and subordinate's economizer import header;Higher level's economizer import header passes through pipeline one and pipeline two connects subordinate and saves
The water route of coal device outlet header, increased the burning area of boiler, improves the efficiency of combustion of boiler, reduces nitrogen oxides
Acquisition rate, finally meets user's requirement, and improves the technical performance of the aspects such as safety, energy-saving and environmental protection, meets
Requirement of the country to environmental protection.
Description of the drawings
Front views of the Fig. 1 for one embodiment of circulating fluid-bed coal-burning boiler energy-saving economizer;
Side views of the Fig. 2 for the embodiment of Fig. 1;
Structural representations of the Fig. 3 for the amplification at the I of Fig. 1;
Structural representations of the Fig. 4 for the amplification at the II of Fig. 2;
Structural representations of the Fig. 5 for the amplification at the III of Fig. 2;
Wherein:1- higher level's economizer, 11- higher level's economizer exit header, the upper the Tubes of Membrane Economizer of 12-, 13- higher level save coal
Device import header;2- SCR catalyst structures, 3- subordinates economizer, 31- subordinates economizer exit header, under 32-, membrane type saves coal
Device pipe, 33- subordinates economizer import header;4- pipelines one, 5- pipelines two, 6- membrane wall pipes, 7- comb plate, comb joints, 8- supports, 9- pots
Furnace body.
Specific embodiment
In order to deepen to understanding of the present utility model, with reference to the accompanying drawings and examples to this utility model furtherly
Bright, the embodiment is only used for explaining this utility model, protection domain of the present utility model is not constituted and is limited.
Circulating fluid-bed coal-burning boiler energy-saving economizer, as shown in figure 1, including the higher level being connected in boiler from top to bottom
Economizer 1, SCR catalyst structure 2 and subordinate's economizer 3, higher level's economizer 1 include that the higher level for setting gradually from top to bottom saves coal
Device outlet header 11, upper the Tubes of Membrane Economizer 12 and higher level's economizer import header 13, under subordinate's economizer 3 includes up to respectively
Subordinate's economizer exit header 31, lower the Tubes of Membrane Economizer 32 for setting gradually and subordinate economizer import header 33;Higher level saves
Coal device import header 13 passes through the water route that pipeline 1 and pipeline 25 connect subordinate economizer exit header 31.
As shown in Fig. 2 and Fig. 3, Fig. 4, upper the Tubes of Membrane Economizer 12 and lower the Tubes of Membrane Economizer 32 are respectively by some row's membrane types
Wall pipe 6 is set up in parallel and forms, and the row of the membrane wall pipe 6 of lower the Tubes of Membrane Economizer 32 is more than the membrane type of upper the Tubes of Membrane Economizer 12
The row of wall pipe 6.
In the above-described embodiments, the row of the membrane wall pipe 6 of upper the Tubes of Membrane Economizer 12 is arranged for 15-20, and lower membrane type saves coal
The row of the membrane wall pipe 6 of device pipe 32 is arranged for 40-45, and total row of upper the Tubes of Membrane Economizer 12 and lower the Tubes of Membrane Economizer 32
Number is 60 rows.As shown in Fig. 2 the preferable one embodiment of economizer province coal effect is after transformation, the upper membrane type of higher level's economizer 1
The height of economizer tube 5 be 17*45=765mm, wherein 17 be row, the height of 45 each rows.And the lower film of subordinate's economizer 3
The height of formula economizer tube 7 is 29*45+13*45=1305+585=1890mm, wherein 29 is the row of the subordinate coal saving tube before transformation
Number, 13 is the coal saving tube that higher level economizer tube is moved.
Referring to Fig. 2 and Fig. 3, connected and fixed by some comb plate, comb joints 7 between the membrane wall pipe 6 of upper the Tubes of Membrane Economizer 12,
Connect and fix also by some comb plate, comb joints 7 between the membrane wall pipe 6 of lower the Tubes of Membrane Economizer 32.
As shown in Figure 2 and Figure 4, upper the Tubes of Membrane Economizer 12 and lower the Tubes of Membrane Economizer 32 are solid by a support 8 respectively
It is scheduled on boiler furnace 9.
Circulating fluid-bed coal-burning boiler energy-saving economizer of the present utility model, in existing boiler economizer, increased
Fore-and-aft distance and heating surface between level economizer and subordinate's economizer, and higher level's economizer 1 includes setting successively from top to bottom
The higher level's economizer exit header 11, upper the Tubes of Membrane Economizer 12 put and higher level's economizer import header 13,3 points of subordinate's economizer
The subordinate's economizer exit header 31, lower the Tubes of Membrane Economizer 32 that up to Bao Kuo do not set gradually down and subordinate's economizer inlet header
Case 33;Higher level's economizer import header 13 passes through the water route that pipeline 1 and pipeline 25 connect subordinate economizer exit header 31,
The burning area of boiler is increased, the efficiency of combustion of boiler is improve, the acquisition rate of nitrogen oxides is reduced, is finally met use
Family requirement, and the technical performance of the aspects such as safety, energy-saving and environmental protection is improve, meet requirement of the country to environmental protection.
What embodiment of the present utility model was announced is preferred embodiment, but is not limited thereto, the common skill of this area
Art personnel, easily according to above-described embodiment, understand spirit of the present utility model, and make different amplifications and change, but as long as
Without departing from spirit of the present utility model, all in protection domain of the present utility model.
Claims (5)
1. circulating fluid-bed coal-burning boiler energy-saving economizer, it is characterised in that:Including the higher level being connected in boiler from top to bottom
Economizer(1), SCR catalyst structure(2)With subordinate's economizer(3), higher level's economizer(1)Including setting successively from top to bottom
The higher level's economizer exit header put(11), upper the Tubes of Membrane Economizer(12)With higher level's economizer import header(13), province of subordinate
Coal device(3)Include the subordinate's economizer exit header for up to setting gradually down respectively(31), lower the Tubes of Membrane Economizer(32)With under
Level economizer import header(33);Higher level's economizer import header(13)By pipeline one(4)With pipeline two(5)Under connection
Level economizer exit header(31)Water route.
2. circulating fluid-bed coal-burning boiler energy-saving economizer according to claim 1, it is characterised in that:The upper membrane type is saved
Coal device pipe(12)With lower the Tubes of Membrane Economizer(32)Respectively by some row's membrane wall pipes(6)It is set up in parallel and forms, the lower membrane type
Economizer tube(32)Membrane wall pipe(6)Row be more than upper the Tubes of Membrane Economizer(12)Membrane wall pipe(6)Row.
3. circulating fluid-bed coal-burning boiler energy-saving economizer according to claim 2, it is characterised in that:The upper membrane type is saved
Coal device pipe(12)Membrane wall pipe(6)Row be 15-20 row, the lower the Tubes of Membrane Economizer(32)Membrane wall pipe(6)'s
Row is arranged for 40-45, and upper the Tubes of Membrane Economizer(12)With lower the Tubes of Membrane Economizer(32)Total row be 60 rows.
4. circulating fluid-bed coal-burning boiler energy-saving economizer according to claim 3, it is characterised in that:The upper membrane type is saved
Coal device pipe(12)Membrane wall pipe(6)Between pass through some comb plate, comb joints(7)Connect and fix, the lower the Tubes of Membrane Economizer(32)'s
Membrane wall pipe(6)Between also by some comb plate, comb joints(7)Connect and fix.
5. the circulating fluid-bed coal-burning boiler energy-saving economizer according to claim 1-4 any one, it is characterised in that:Institute
State the Tubes of Membrane Economizer(12)With lower the Tubes of Membrane Economizer(32)Pass through a support respectively(8)It is fixed on boiler furnace(9)
On.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621002520.7U CN206094053U (en) | 2016-08-31 | 2016-08-31 | Energy -conserving economizer of bed coal fired boiler is vulcanized in circulation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621002520.7U CN206094053U (en) | 2016-08-31 | 2016-08-31 | Energy -conserving economizer of bed coal fired boiler is vulcanized in circulation |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206094053U true CN206094053U (en) | 2017-04-12 |
Family
ID=58477524
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621002520.7U Withdrawn - After Issue CN206094053U (en) | 2016-08-31 | 2016-08-31 | Energy -conserving economizer of bed coal fired boiler is vulcanized in circulation |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206094053U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106196033A (en) * | 2016-08-31 | 2016-12-07 | 江苏汇能锅炉有限公司 | Circulating fluid-bed coal-burning boiler energy-saving economizer |
-
2016
- 2016-08-31 CN CN201621002520.7U patent/CN206094053U/en not_active Withdrawn - After Issue
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106196033A (en) * | 2016-08-31 | 2016-12-07 | 江苏汇能锅炉有限公司 | Circulating fluid-bed coal-burning boiler energy-saving economizer |
CN106196033B (en) * | 2016-08-31 | 2019-04-30 | 江苏汇能锅炉有限公司 | Circulating fluid-bed coal-burning boiler energy-saving economizer |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203628635U (en) | Supercritical circulating fluidized bed boiler | |
CN202141027U (en) | Environment-friendly energy-saving biomass hot pipe boiler | |
CN103047643A (en) | Energy-saving type circulating fluidized bed boiler for combusting lower-calorific value fuel | |
CN104456545A (en) | Special circulating fluidized bed boiler with flue gas recirculation | |
CN206094053U (en) | Energy -conserving economizer of bed coal fired boiler is vulcanized in circulation | |
CN204420993U (en) | With the specific cycle fluidized-bed combustion boiler of flue gas recirculation | |
CN206094052U (en) | Bed coal fired boiler economizer is vulcanized in high -efficient circulation | |
CN101963350A (en) | Material separator for circulating fluidized bed boiler | |
CN106287680A (en) | Small-sized biomass shaped fuel recirculating fluidized bed steam boiler | |
CN2711540Y (en) | Low circulation multiplying factor low smoke speed intermediate temperature separation circulating fluidized bed boiler | |
CN106196033B (en) | Circulating fluid-bed coal-burning boiler energy-saving economizer | |
CN202733916U (en) | Burning dregs fluidized bed boiler | |
CN103486574B (en) | Large-scale low First air power consumption supercritical circulating fluidized bed boiler | |
CN106247324B (en) | Efficient circulating fluid bed coal-burning boiler coal economizer | |
CN109058983A (en) | Recirculating fluidized bed combustion with meagre oxygen catalysis oxidation fractional combustion boiler system and method | |
CN204514070U (en) | A kind of sinter fume waste heat recovery horizontal type waste heat boiler | |
CN106439798B (en) | Circulating fluid-bed coal-burning boiler economizer | |
CN209541168U (en) | Coal dust organic heat carrier furnace in bulk | |
CN207990606U (en) | A kind of boiler is for exhaust system | |
CN208124332U (en) | A kind of energy-saving boiler system | |
CN105444144A (en) | 300MWCFB boiler and distribution method for oil shale for combustion | |
CN106287683B (en) | Circulating fluidized bed combustion coal boiler economizer energy-conserving reconstruction method | |
CN205155925U (en) | Biomass boiler afterbody residual heat from flue gas system | |
CN215112568U (en) | Coal gangue component activation high-temperature furnace | |
CN104251487A (en) | Method for improving boiler combustion economy of tangential combustion anthracite coal boiler |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20170412 Effective date of abandoning: 20190430 |
|
AV01 | Patent right actively abandoned |