CN109210556A - A kind of residual neat recovering system - Google Patents

A kind of residual neat recovering system Download PDF

Info

Publication number
CN109210556A
CN109210556A CN201710530033.0A CN201710530033A CN109210556A CN 109210556 A CN109210556 A CN 109210556A CN 201710530033 A CN201710530033 A CN 201710530033A CN 109210556 A CN109210556 A CN 109210556A
Authority
CN
China
Prior art keywords
flashboard
branch
sensor
recovering system
unit
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.)
Pending
Application number
CN201710530033.0A
Other languages
Chinese (zh)
Inventor
何亮
王鹏起
武发德
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing New Building Material Group Co Ltd
Original Assignee
Beijing New Building Material Group Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beijing New Building Material Group Co Ltd filed Critical Beijing New Building Material Group Co Ltd
Priority to CN201710530033.0A priority Critical patent/CN109210556A/en
Publication of CN109210556A publication Critical patent/CN109210556A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/06Arrangements of devices for treating smoke or fumes of coolers
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Abstract

A kind of residual neat recovering system, including desulfurizing tower, pipe-line cell, power unit and control unit are disclosed herein;Wherein, the beginning of the pipe-line cell connects the smoke outlet of the desulfurizing tower, and end connects battery limits to be heated;The power unit is arranged in the pipe-line cell, and the power unit is used for the control signalizing activity according to described control unit, to guide the flue gas at the smoke outlet to be delivered to target position;The application can be applied to heat recovery field, can effectively overcome defect in the prior art using the application, can effectively utilize the smoke backflow of desulfurizing tower, can be effectively reduced production cost.

Description

A kind of residual neat recovering system
Technical field
This application involves but be not limited to heat recovery field, especially a kind of residual neat recovering system.
Background technique
Currently, proposing in " 13 " energy-saving and emission-reduction synthetic operation scheme, to reinforce industrial energy saving, arrive the year two thousand twenty, industry It efficiency of energy utilization and cleans level and significantly improves, the reduction in than 2015 of state-owned and large non-state industrial enterprises' unit value added energy consumption 18% or more.Wherein, in plasterboard industrial processes, the hot fume that former hot shop generates after desulfurizing tower desulfurization process, Temperature causes the waste of thermal energy in 50-70 DEG C of flue gas direct emission.
Therefore, for active response national energy conservation and emission reduction policy, how desulfurizing tower outlet hot fume to be recycled and is used in life It produces, it is urgent problem that reaching, which reduces production cost purpose,.
Summary of the invention
The technical issues of the application solves is to provide a kind of residual neat recovering system, can effectively overcome in the prior art lack It falls into, effectively the smoke backflow of desulfurizing tower can be utilized, can be effectively reduced production cost.
In order to solve the above technical problems, this application provides a kind of residual neat recovering system, including desulfurizing tower, it further include pipeline Unit, power unit and control unit;Wherein,
The beginning of the pipe-line cell connects the smoke outlet of the desulfurizing tower, and end connects battery limits to be heated;
The power unit is arranged in the pipe-line cell, and the power unit is used for the control according to described control unit Signalizing activity processed, to guide the flue gas at the smoke outlet to be delivered to target position.
Above-mentioned residual neat recovering system can also have a characteristic that
It further include detection unit;
The detection unit is used to detect the oxygen content in the pipe-line cell, and detects the battery limits to be heated Oxygen content, and will test signal and be conveyed to described control unit;
Described control unit is used to export corresponding control signal according to the detection signal.
Above-mentioned residual neat recovering system can also have a characteristic that
It further include flashboard unit;
The flashboard unit is arranged in the pipe-line cell, and described control unit is also used to control the flashboard unit Flashboard aperture.
Above-mentioned residual neat recovering system can also have a characteristic that
The battery limits to be heated include fluidized bed furnace and discharge tank, and the pipe-line cell includes the first branch, second branch With third branch;
The beginning of the first branch connects the smoke outlet of the desulfurizing tower, the end connection of the first branch described the The beginning of two branches, third branch, the end of the second branch connect the air blower of the fluidized bed furnace, the third branch End connects the discharge tank.
Above-mentioned residual neat recovering system can also have a characteristic that
The detection unit includes first sensor and second sensor, and the first sensor is arranged in the fluidized bed furnace Bellows in, the second sensor is arranged in the second branch.
Above-mentioned residual neat recovering system can also have a characteristic that
The flashboard unit includes the first flashboard and the second flashboard, and the first flashboard setting is on the first leg, described Second flashboard is arranged in the second branch.
Above-mentioned residual neat recovering system can also have a characteristic that
The power unit is set as air-introduced machine, the driving electricity that described control unit passes through control circuit and the air-introduced machine Machine connection.
Above-mentioned residual neat recovering system can also have a characteristic that
First flashboard, the second flashboard are disposed as electric brake plate valve, and described control unit is distinguished by control circuit Connect the electric brake plate valve.
Above-mentioned residual neat recovering system can also have a characteristic that
Side of the power unit far from smoke outlet is arranged in first flashboard, and second flashboard is arranged described Side of the second sensor far from bellows.
Above-mentioned residual neat recovering system can also have a characteristic that
The first sensor, second sensor are disposed as determination of oxygen content sensor, and described control unit passes through control Circuit processed is separately connected the determination of oxygen content sensor.
The application above-mentioned technical proposal has the following beneficial effects:
Compared with the prior art, the application can be capable of providing by the setting of above-mentioned pipe-line cell to the flue gas of desulfurizing tower Fixed conveyance conduit is discharged, to realize effective conveying of flue gas;It can be can effectively ensure that by the setting of above-mentioned power unit The transfer efficiency of flue gas at the smoke outlet of desulfurizing tower can drive flue gas to be endlessly delivered to from the smoke outlet of desulfurizing tower Battery limits to be heated;Effective control of power unit can be can be realized, according to practical feelings by the setting of above-mentioned control unit Condition carries out corresponding power adjustment, to realize different transfer efficiencies.
Further, the application can also be guided the discharged gas fume of desulfurizing tower by the setting of the above-mentioned first branch At to the connection prong of second branch and third branch;Can be by the setting of above-mentioned second branch, it can will be in the first branch Flue gas is delivered at the air blower of fluidized bed furnace, after backflow flue gas and cold air mixing, can be improved blast temperature, and can satisfy Oxygen needed for boiling furnace combustion and air quantity;Can be by the setting of above-mentioned third branch, it can be defeated by the flue gas in the first branch It send to discharge tank, backflow flue gas replaces fresh cold air cooling to the material in calciner discharge tank, can be effectively reduced Heat loss, and then save coal consumption;Above-mentioned multiple branches are preferably provided with, and can utilize the smoke backflow of desulfurizing tower outlet, from And realize Waste Heat Reuse, energy saving advantageous effects.
Further, the application can also be by control unit according to first sensor, the testing result of second sensor, control Make the first flashboard, the second flashboard executes the operation of corresponding aperture, enable to the oxygen content in bellows to maintain normal level It is interior, can effectively avoid because the oxygen content in bellows it is excessively high or too low caused by combustion instability, or burning it is insufficient Defect, actual efficiency of combustion can be effectively improved.
Other features and advantage will illustrate in the following description, also, partly become from specification It obtains it is clear that being understood by implementing the embodiment of the present invention.The purpose of the application and other advantages can be by illustrating Specifically noted structure is achieved and obtained in book, claims and attached drawing.
Detailed description of the invention
Attached drawing is used to provide to further understand technical scheme, and constitutes part of specification, with this The embodiment of application is used to explain the technical solution of the application together, does not constitute the limitation to technical scheme.
Fig. 1 is the structural schematic diagram of the embodiment of the present invention one;
It illustrates:
1- desulfurizing tower, 2- fluidized bed furnace, 3- bellows, 4- air blower, 5- discharge tank, 6- power unit, 7- second sensor, 8- First sensor, the 9- first branch, 10- third branch, 11- second branch, the first flashboard of 12-, the second flashboard of 13-.
Specific embodiment
Embodiments herein is described in detail below in conjunction with attached drawing.It should be noted that not conflicting In the case of, the features in the embodiments and the embodiments of the present application can mutual any combination.
Embodiment one:
As shown in connection with fig. 1, the embodiment of the present invention one provides a kind of residual neat recovering system, including desulfurizing tower 1, further includes pipe Road unit, power unit 6 and control unit;Wherein, the smoke outlet of the beginning connection desulfurizing tower 1 of pipe-line cell, end connection Battery limits to be heated;Power unit 6 is arranged in pipe-line cell, and power unit 6 is used for dynamic according to the control signal of control unit Make, to guide the flue gas at smoke outlet to be delivered to target position.
In concrete operations, it can be capable of providing by the setting of above-mentioned pipe-line cell to the flue gas emission fixation of desulfurizing tower 1 Conveyance conduit, to realize effective conveying of flue gas;It can effectively ensure that desulfurizing tower 1 by the setting of above-mentioned power unit 6 The transfer efficiency of flue gas at smoke outlet can drive flue gas to be endlessly delivered to from the smoke outlet of desulfurizing tower 1 to be heated Battery limits;Effective control of power unit 6 can be can be realized by the setting of above-mentioned control unit, with according to the actual situation, into The corresponding power adjustment of row, to realize different transfer efficiencies.
Preferably, in the present embodiment, residual neat recovering system further includes detection unit;Detection unit is for detecting the pipeline The oxygen content of oxygen content and the battery limits to be heated in unit, and will test signal and be conveyed to control unit;Control is single Member is for according to the corresponding control signal of detection signal output.
In the present embodiment, above-mentioned battery limits to be heated include fluidized bed furnace 2 and discharge tank 5, and pipe-line cell includes the first branch 9, second branch 11 and third branch 10;The smoke outlet of the beginning connection desulfurizing tower 1 of the first branch 9, the end of the first branch 9 connects Connect the beginning of second branch 11, third branch 10, the air blower 4 of the end connection fluidized bed furnace 2 of second branch 11, third branch 10 End connect discharge tank 5.
In concrete operations, the setting of the above-mentioned first branch 9 can guide the discharged gas fume of desulfurizing tower 1 to second branch 11 and third branch 10 connection prong at, i.e., diagram in T word connect nozzle position;The setting of above-mentioned second branch 11, energy It is enough that flue gas in the first branch 9 is delivered at the air blower 4 of fluidized bed furnace 2, after backflow flue gas and cold air mixing, it can be improved Blast temperature, and can satisfy fluidized bed furnace 2 and burn required oxygen and air quantity;The setting of above-mentioned third branch 10, can be by Flue gas in one branch 9 is delivered at discharge tank 5, and backflow flue gas replaces fresh cold air to the object in calciner discharge tank 5 Material cooling can be effectively reduced heat loss, and then save coal consumption;Above-mentioned multiple branches are preferably provided with, can will be outside desulfurizing tower 1 The smoke backflow of row utilizes, thus realize Waste Heat Reuse, energy saving advantageous effects.
Preferably, in the present embodiment, above-mentioned residual neat recovering system further includes flashboard unit, and flashboard unit is arranged in pipeline list In member, control unit is also used to control the flashboard aperture of flashboard unit.
In concrete operations, above-mentioned flashboard unit includes the first flashboard 12 and the second flashboard 13, and the setting of the first flashboard 12 is the On one branch 9, the second flashboard 13 is arranged in second branch 11;Above-mentioned first flashboard 12, the second flashboard 13 are disposed as electronic Slide valve, control unit are separately connected electric brake plate valve by control circuit;Above-mentioned control circuit can be by controlling the first flashboard 12 opening size, and then control the total amount of the conveying gas of the first branch 9;Correspondingly, above-mentioned control circuit can also pass through control The opening size of the second flashboard 13 is made, and then controls the total amount of the conveying gas of second branch 11, that is, is delivered at air blower 4 Amount of flue gas emission.
In order to realize effective control of the conveying gas in the first branch 9 and second branch 11, in the present embodiment, on It states the first flashboard 12 and side of the power unit 6 far from smoke outlet is set, the second flashboard 13 is arranged in second sensor 7 far from wind The side of case 3.
Preferably, in the present embodiment, above-mentioned detection unit includes first sensor 8 and second sensor 7, first sensor 8 are arranged in the bellows 3 of fluidized bed furnace 2, and second sensor 7 is arranged in second branch 11.In concrete operations, above-mentioned first sensing Device 8, second sensor 7 are disposed as determination of oxygen content sensor, and control unit is separately connected oxygen content by control circuit and surveys Determine sensor.
When the oxygen content in the bellows 3 that first sensor 8 detects fluidized bed furnace 2, second sensor 7 detect second When oxygen content in road 11 is all larger than preset value, show that the oxygen proportion in bellows 3 at this time is excessively high, control circuit produces phase The control signal answered, to control the aperture for reducing the second flashboard 13, so that more flue gas enters third branch 10;Alternatively, control Circuit processed also can control the aperture for reducing the first flashboard 12, i.e., reduces from the total amount of source control flue gas, so that into bellows 3 Flue gas it is less, advantageously reduce the oxygen content in bellows 3, maintain it in normal level.
When the oxygen content in the bellows 3 that first sensor 8 detects fluidized bed furnace 2, second sensor 7 detect second When oxygen content in road 11 is respectively less than preset value, show that the oxygen proportion in bellows 3 at this time is too low;Control method and aforementioned side Method is similar, it is intended to the aperture for reducing the second flashboard 13 is controlled by control circuit, so that more flue gas enters third branch 10; Alternatively, control circuit also can control the aperture for reducing the first flashboard 12, i.e., reduced from the total amount of source control flue gas, so that into Flue gas in bellows 3 is less, advantageously reduces the oxygen content in bellows 3, maintains it in normal level.
When the oxygen content in the bellows 3 that first sensor 8 detects fluidized bed furnace 2 is greater than preset value, and second sensor 7 When detecting that the oxygen content in second branch 11 is less than preset value, show that the oxygen proportion in bellows 3 at this time is higher, second Oxygen proportion in road 11 is lower;Control circuit produces corresponding control signal, to control the aperture for increasing the second flashboard 13, So that more flue gas enters second branch 11, and enter in bellows 3, so that the gas mixing of two kinds of different oxygen contents is equal It is even, so that the oxygen content in bellows 3 maintains in normal level.
When the oxygen content in the bellows 3 that first sensor 8 detects fluidized bed furnace 2 is less than preset value, and second sensor 7 When detecting that the oxygen content in second branch 11 is greater than preset value, show that the oxygen proportion in bellows 3 at this time is lower, second Oxygen proportion in road 11 is higher;Control method is similar with preceding method, it is intended to be controlled by control circuit and increase the second flashboard 13 aperture so that more flue gas enters second branch 11, and enters in bellows 3, so that the gas of two kinds of different oxygen contents Body is uniformly mixed, so that the oxygen content in bellows 3 maintains in normal level.
In concrete operations, the PLC programmable logic controller (PLC) that above-mentioned control unit can be common using this field, by setting Different threshold values is set, to realize corresponding convenient control operation.
Preferably, in the present embodiment, above-mentioned power unit 6 is set as air-introduced machine, and control unit passes through control circuit and draws The driving motor of blower connects.
In concrete operations, above-mentioned driving motor can cooperate aforementioned first sensor 8 and second sensor 7 to apply, i.e., when need When controlling the aperture that the second flashboard 13 is decreased or increased, can also simultaneous selection control turn down or be turned up the revolving speed of driving motor, With within the shortest time, so that the oxygen content in bellows 3 maintains in normal level.
One record is it is found that the application can be capable of providing by the setting of above-mentioned pipe-line cell to desulfurization in conjunction with the embodiments The fixed conveyance conduit of the flue gas emission of tower, to realize effective conveying of flue gas;Can be by the setting of above-mentioned power unit, it can The transfer efficiency of the flue gas at the smoke outlet of desulfurizing tower is effectively ensured, can drive flue gas endlessly from the smoke evacuation of desulfurizing tower Mouth is delivered to battery limits to be heated;Effective control of power unit can be can be realized, by the setting of above-mentioned control unit with root According to actual conditions, corresponding power adjustment is carried out, to realize different transfer efficiencies.
Further, the application can also be guided the discharged gas fume of desulfurizing tower by the setting of the above-mentioned first branch At to the connection prong of second branch and third branch;Can be by the setting of above-mentioned second branch, it can will be in the first branch Flue gas is delivered at the air blower of fluidized bed furnace, after backflow flue gas and cold air mixing, can be improved blast temperature, and can satisfy Oxygen needed for boiling furnace combustion and air quantity;Can be by the setting of above-mentioned third branch, it can be defeated by the flue gas in the first branch It send to discharge tank, backflow flue gas replaces fresh cold air cooling to the material in calciner discharge tank, can be effectively reduced Heat loss, and then save coal consumption;Above-mentioned multiple branches are preferably provided with, and can utilize the smoke backflow of desulfurizing tower outlet, from And realize Waste Heat Reuse, energy saving advantageous effects.
Further, the application can also be by control unit according to first sensor, the testing result of second sensor, control Make the first flashboard, the second flashboard executes the operation of corresponding aperture, enable to the oxygen content in bellows to maintain normal level It is interior, can effectively avoid because the oxygen content in bellows it is excessively high or too low caused by combustion instability, or burning it is insufficient Defect, actual efficiency of combustion can be effectively improved.
In the description of the present application, term " installation ", " connected ", " connection ", " fixation " etc. be shall be understood in a broad sense, example Such as, " connection " may be fixed connection or may be dismantle connection, or integral connection;It can be directly connected, it can also be with Indirectly connected through an intermediary.For the ordinary skill in the art, above-mentioned art can be understood as the case may be The concrete meaning of language in this application.
In the description of this specification, the description of term " one embodiment ", " some embodiments ", " specific embodiment " etc. Mean that particular features, structures, materials, or characteristics described in conjunction with this embodiment or example are contained at least one reality of the application It applies in example or example.In the present specification, schematic expression of the above terms are not necessarily referring to identical embodiment or reality Example.Moreover, description particular features, structures, materials, or characteristics can in any one or more of the embodiments or examples with Suitable mode combines.
Although those skilled in the art should be understood that embodiment disclosed by the embodiment of the present invention is as above, described The content only embodiment of the present invention and the embodiment that uses for ease of understanding, be not intended to limit the invention embodiment.It is any Technical staff in fields of the embodiment of the present invention, in the premise for not departing from spirit and scope disclosed by the embodiment of the present invention Under, any modification and variation, but the scope of patent protection of the embodiment of the present invention can be carried out in the form and details of implementation, Still it should be subject to the scope of the claims as defined in the appended claims.

Claims (10)

1. a kind of residual neat recovering system, including desulfurizing tower, which is characterized in that further include pipe-line cell, power unit and control Unit;Wherein,
The beginning of the pipe-line cell connects the smoke outlet of the desulfurizing tower, and end connects battery limits to be heated;
The power unit is arranged in the pipe-line cell, and the power unit is used to be believed according to the control of described control unit Number movement, to guide the flue gas at the smoke outlet to be delivered to target position.
2. residual neat recovering system according to claim 1, which is characterized in that further include detection unit;
The detection unit is used to detect the oxygen content in the pipe-line cell, and detects the oxygen-containing of the battery limits to be heated Amount, and will test signal and be conveyed to described control unit;
Described control unit is used to export corresponding control signal according to the detection signal.
3. residual neat recovering system according to claim 2, which is characterized in that further include flashboard unit;
The flashboard unit is arranged in the pipe-line cell, and described control unit is also used to control the flashboard of the flashboard unit Aperture.
4. residual neat recovering system according to claim 3, which is characterized in that
The battery limits to be heated include fluidized bed furnace and discharge tank, and the pipe-line cell includes the first branch, second branch and Three branches;
The beginning of the first branch connects the smoke outlet of the desulfurizing tower, described second of the end connection of the first branch Road, third branch beginning, the end of the second branch connects the air blower of the fluidized bed furnace, the end of the third branch Connect the discharge tank.
5. residual neat recovering system according to claim 4, which is characterized in that
The detection unit includes first sensor and second sensor, and the wind of the fluidized bed furnace is arranged in the first sensor In case, the second sensor is arranged in the second branch.
6. residual neat recovering system according to claim 5, which is characterized in that
The flashboard unit includes the first flashboard and the second flashboard, and first flashboard is arranged on the first leg, and described second Flashboard is arranged in the second branch.
7. any residual neat recovering system in -6 according to claim 1, which is characterized in that
The power unit is set as air-introduced machine, and described control unit is connected by the driving motor of control circuit and the air-introduced machine It connects.
8. residual neat recovering system according to claim 6, which is characterized in that
First flashboard, the second flashboard are disposed as electric brake plate valve, and described control unit is separately connected by control circuit The electric brake plate valve.
9. residual neat recovering system according to claim 6, which is characterized in that
Side of the power unit far from smoke outlet is arranged in first flashboard, and second flashboard is arranged described second Side of the sensor far from bellows.
10. residual neat recovering system according to claim 5, which is characterized in that
The first sensor, second sensor are disposed as determination of oxygen content sensor, and described control unit passes through control electricity Road is separately connected the determination of oxygen content sensor.
CN201710530033.0A 2017-06-30 2017-06-30 A kind of residual neat recovering system Pending CN109210556A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710530033.0A CN109210556A (en) 2017-06-30 2017-06-30 A kind of residual neat recovering system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710530033.0A CN109210556A (en) 2017-06-30 2017-06-30 A kind of residual neat recovering system

Publications (1)

Publication Number Publication Date
CN109210556A true CN109210556A (en) 2019-01-15

Family

ID=64992234

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710530033.0A Pending CN109210556A (en) 2017-06-30 2017-06-30 A kind of residual neat recovering system

Country Status (1)

Country Link
CN (1) CN109210556A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN203874324U (en) * 2014-04-16 2014-10-15 西安西热锅炉环保工程有限公司 System for extracting low-temperature boiler smoke and making raw coal in spherical coal bunker inert to prevent raw coal from oxidative spontaneous combustion
KR20150123492A (en) * 2014-04-25 2015-11-04 한국타이어 주식회사 Heating system using waste gas of tire vulcanizer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN203874324U (en) * 2014-04-16 2014-10-15 西安西热锅炉环保工程有限公司 System for extracting low-temperature boiler smoke and making raw coal in spherical coal bunker inert to prevent raw coal from oxidative spontaneous combustion
KR20150123492A (en) * 2014-04-25 2015-11-04 한국타이어 주식회사 Heating system using waste gas of tire vulcanizer

Similar Documents

Publication Publication Date Title
CN104229855B (en) Utilize electricity generation boiler or the technique of sintering device flue gas on-line heating oxidation sweetening ash
CN104034175A (en) Energy-saving and emission-reducing type sintering process
CN109114588A (en) It is pure to fire high-alkali coal wet bottom boiler low NOx combustion system and method for controlling combustion
KR20140000125A (en) Exhaust gas recycling control system of combustion device
CN109813094B (en) Multi-effect rapid alloy material baking and preheating device and using method thereof
CN103940213A (en) Coke drying system dry gas temperature and flow self-adjustment control device and method
CN202216277U (en) Automatic control device for a combustor type industrial boiler
CN102353073A (en) Automatic control method for burner type industrial boiler and device for automatic control method
CN103968409B (en) A kind of high-temperature and low-oxygen combustion device
CN201706903U (en) Device used for controlling internal pressure of furnace and recovering heat energy of flue gas
CN205874470U (en) Blast funnace hot blast stove optimal control system
CN109210556A (en) A kind of residual neat recovering system
CN204943510U (en) A kind of tail gas from electric furnace energy-saving emission-reducing apparatus
CN204007178U (en) Heat-treatment furnace flue gas waste heat utilization device
CN209130922U (en) The pure high-alkali coal wet bottom boiler low NOx combustion system of combustion
CN103822498A (en) Kiln waste heat recycling device
CN208952122U (en) A kind of device reducing the nitrogen oxides in flue gases of cock oven by waste gas circulation
CN201521944U (en) Waste-heat boiler off-gas control apparatus for float glass smelting kiln
CN201488567U (en) Energy-saving device utilizing smoke of kiln for supplying heat to spray tower
CN205897122U (en) Circulating fluidized bed boiler fly ash recycle system
CN205481567U (en) A economizer system that is used for clean laboratory to keep constant voltage
CN108036653A (en) A kind of energy-saving and environment-friendly cast stone production smoke circulating system
CN206018595U (en) Chain grate boiler compound combustion control system
CN205582634U (en) A gas baker for enameled wire is made
CN109210554A (en) A kind of desulfurizing tower low-temperature flue gas reclaimer

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20190115

RJ01 Rejection of invention patent application after publication