US20100307393A1 - Stoker-fired boiler, a method of modernization of stoker-fired boilers and a method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler - Google Patents

Stoker-fired boiler, a method of modernization of stoker-fired boilers and a method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler Download PDF

Info

Publication number
US20100307393A1
US20100307393A1 US12/734,889 US73488908A US2010307393A1 US 20100307393 A1 US20100307393 A1 US 20100307393A1 US 73488908 A US73488908 A US 73488908A US 2010307393 A1 US2010307393 A1 US 2010307393A1
Authority
US
United States
Prior art keywords
stoker
wind boxes
air
channel
air channel
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.)
Abandoned
Application number
US12/734,889
Inventor
Witold Kowalewski
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of US20100307393A1 publication Critical patent/US20100307393A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23HGRATES; CLEANING OR RAKING GRATES
    • F23H11/00Travelling-grates
    • F23H11/10Travelling-grates with special provision for supply of air from below and for controlling air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B1/00Combustion apparatus using only lump fuel
    • F23B1/16Combustion apparatus using only lump fuel the combustion apparatus being modified according to the form of grate or other fuel support
    • F23B1/22Combustion apparatus using only lump fuel the combustion apparatus being modified according to the form of grate or other fuel support using travelling grate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B30/00Combustion apparatus with driven means for agitating the burning fuel; Combustion apparatus with driven means for advancing the burning fuel through the combustion chamber
    • F23B30/02Combustion apparatus with driven means for agitating the burning fuel; Combustion apparatus with driven means for advancing the burning fuel through the combustion chamber with movable, e.g. vibratable, fuel-supporting surfaces; with fuel-supporting surfaces that have movable parts
    • F23B30/06Combustion apparatus with driven means for agitating the burning fuel; Combustion apparatus with driven means for advancing the burning fuel through the combustion chamber with movable, e.g. vibratable, fuel-supporting surfaces; with fuel-supporting surfaces that have movable parts with fuel supporting surfaces that are specially adapted for advancing fuel through the combustion zone
    • F23B30/08Combustion apparatus with driven means for agitating the burning fuel; Combustion apparatus with driven means for advancing the burning fuel through the combustion chamber with movable, e.g. vibratable, fuel-supporting surfaces; with fuel-supporting surfaces that have movable parts with fuel supporting surfaces that are specially adapted for advancing fuel through the combustion zone with fuel-supporting surfaces that move through the combustion zone, e.g. with chain grates

Definitions

  • the subject of the invention is a stoker-fired boiler containing in the combustion zone a movable stoker and an under-stoker wind boxes system, a method of modernization of such a boiler as well as a method of elimination of uncontrolled leakages of air not taking part in the combustion process in the boiler.
  • the pressure is close to the pressure in the combustion chamber, and usually amounts to some ⁇ 30 to ⁇ 50 Pa.
  • the appearing differences in pressure between the wind box spaces, the under-stoker space, and the atmosphere cause flows of uncontrolled leakages of air streams through the gaps existing between these spacer, however prober manufacturing of a boiler does not ensure its complete tightness.
  • Sealing of the said spaces in a stoker-fired boiler meaning the elimination of uncontrolled leakages of air not taking part in the solid fuel combustion process, was subject of many solutions and attempts. From the Polish patent No. 183654 description, it is known that a stoker-fired boiler burner has already been sealed by means of metallic membrane walls.
  • Migration of air streams within a stoker-fired boiler may also be controlled through the appropriate shaping of wind boxes of the under-stoker wind boxes system.
  • the purpose of the invention was to reduce uncontrolled flows of air streams within a stoker-fired boiler, negatively affecting its performance.
  • a boiler according to the invention contains an combustion chamber with a secondary air channel, a movable mechanical stoker, and an under-stoker space containing an under-stoker wind boxes system with wind boxes, as well as a channel supplying the air into the inside of the wind boxes
  • the essence of the invention is that the boiler contains an additional air channel with an inbuilt fan with adjustable output. One end of this additional air channel is connected with the under-stoker space located outside of the wind boxes of the under-stoker wind boxes system.
  • the other end of the additional air channel is connected with either the space of the channel supplying the external air to the wind boxes of the under-stoker wind boxes system, or with the atmosphere or with the secondary air channel of the combustion chamber.
  • At least one air temperature sensor in the space of the channel supplying the air from the atmosphere to the inside of the wind boxes as well as in the space of the additional air channel is located at least one air temperature sensor. These sensors may be connected to controller of the fan of the additional air channel.
  • a method of modernization according to the invention consists in that the under-stoker space of the aforementioned boiler, located outside of the wind boxes of the under-stoker wind boxes system, is connected with the first end of the additional air channel having an inbuilt fan with adjustable output.
  • the other end of the additional air channel is connected with either the space of the channel supplying the air to the wind boxes of the under-stoker wind boxes system, or with the atmosphere or with the secondary air channel of the combustion chamber.
  • At least one air temperature sensor in the space of the channel supplying the air from the atmosphere to the inside of the wind boxes, as well as in the space of the additional air channel is located at least one air temperature sensor. These sensors may be connected to the controller of the fan of the additional air channel.
  • the method of elimination of uncontrolled air leakages consists in leading out and air from the under-stoker space of a boiler, located outside of the wind boxes of the under-stoker wind boxes system, to an additional air channel having an inbuilt fan with changeable output. Current output of this fan is proportional to the current difference between temperature of air supplied to the wind boxes, and the temperature of air in the additional air channel.
  • the air led out to the additional air channel is either supplied to the wind boxes of the under-stoker wind boxes system, or is led out further into the atmosphere, or supplied to the secondary air channel of the combustion chamber of the boiler.
  • the invention reduces the amount of air coming through the gaps and combining with the combustion fumes, giving in consequence a reduced coefficient of excess air in the fumes. This results in a reduction of a physical loss in the fumes, which also means the increase of boiler performance, usually by about 2 to 5%, depending on its technical condition, changes of the load, quality of the combustion charge, and proper maintenance and operation.
  • the application of the invention also reduces the consumption of electric power by the components of the boiler by approximately 10-20%.
  • the load of the extractor fan is smaller, and the consumption of energy by the fan of the additional air channel is balanced by limited energy consumption by the wind boxes air fan.
  • a beneficial feature of the invention is also a short time needed for the modernization of the boiler, and a low cost of such modernization that amounts to ca. 10% of the cost of replacement of the under-stoker wind boxes system.
  • the invention has been shown in a drawing, presenting schematic vertical cross sections of a stoker-fired boiler, whereas
  • FIG. 1 presents a boiler with the first variant of an additional air channel
  • FIG. 2 presents a boiler with the second variant of this channel
  • FIG. 3 presents a boiler with the third variant of such a channel.
  • a typical stoker-fired boiler has a fume zone with a fume extractor fan 1 , and a burner zone.
  • the burner zone there is an combustion chamber 2 , a movable mechanical stoker 3 , an under-stoker wind boxes system 4 with wind boxes 5 , and a channel 6 supplying the air from the atmosphere to the inside of the wind boxes 5 by means of a wind boxes air fan 7 .
  • the combustion chamber 2 has a secondary air channel powered by a fan 8 .
  • the boiler according to the invention has an additional air channel 9 with an inbuilt fan 10 with adjustable output. One end 9 ′ of the additional air channel 9 is connected with the under-stoker space 11 located outside of the wind boxes 5 of the under-stoker wind boxes system 4 .
  • the other end 9 ′′ of the additional air channel 9 may be connected with either the space of channel 6 supplying external air to the wind boxes 5 of the under-stoker wind boxes system 4 , or with the atmosphere or with the secondary air channel of the combustion chamber 2 .
  • Through controlling the output of the fan 10 an appropriate amount of air deriving from uncontrolled leakages is removed from the under-stoker zone 11 , and directed to a selected place via the additional air channel 9 .
  • Output of the fan 10 may be controlled manually, whereas it is beneficial to use for this purpose the knowledge of air temperature in the space of channel 6 supplying it from the atmosphere to the inside of the wind boxes 5 , and temperature of the air in the space of the additional air channel 9 .
  • At least one air temperature sensor (not shown in the drawings) should be placed.
  • the difference between the temperature of wind boxes air stream in the channel 6 , and temperature of air stream in the additional air channel 9 not exceeding 5° C. shows that through channel 9 flows only the air coming from uncontrolled leakages to the under-stoker space.
  • the difference in temperatures amounting to 5 to 10° C. constitutes information that in the additional air channel 9 there also is the air deriving from uncontrolled leakages taking place through the section of the stoker 3 on which the combustion process no longer takes place or takes place into a limited extent.

Abstract

A boiler according to the invention contains an additional air channel (9) with an inbuilt fan (10) with adjustable output. The first end (91) of the additional air channel (9) is connected with the under-stoker space (11) located outside of the wind boxes (5) of the under-stoker wind boxes system (4). The other end (9′) of the additional air channel (9) is connected with either the space of the channel (6) supplying outside air to the wind boxes (5) or with the atmosphere or with the secondary air channel of the combustion chamber (2). Modernization of the existing boilers consists in installation in the described above method of an additional air channel (9) with an inbuilt fan (10). The method of elimination of uncontrolled leakages in a stoker-fired boiler consist in leading out and air, getting through air gaps, from the under-stoker space of the boiler located outside of the wind boxes (5) to the described above additional air channel (6), wherein current output of the fan (10) built into this channel is proportional to the current difference between temperature of air supplied to the wind boxes (5) and temperature of air in the additional air channel (6).

Description

    TECHNICAL FIELD
  • The subject of the invention is a stoker-fired boiler containing in the combustion zone a movable stoker and an under-stoker wind boxes system, a method of modernization of such a boiler as well as a method of elimination of uncontrolled leakages of air not taking part in the combustion process in the boiler.
  • BACKGROUND ART
  • In the commercial power industry and heating industry, for generating heat stoker-fired boilers are commonly employed, in which the combustion of solid fuel, in particular of coal, takes place on a moving mechanical stoker. Above the stoker there is an combustion chamber with a secondary air channel, whereas under the stoker there is an under-stoker space containing the under-stoker wind boxes system with wind boxes, and a channel supplying the air from the atmosphere to the inside of the wind boxes, which is necessary for the combustion process on the stoker to take place. During utilization of the boiler, in the wind box spaces, the air pressure usually amounts to approximately 200-500 Pa. In the remaining part of the under-stoker space, the pressure is close to the pressure in the combustion chamber, and usually amounts to some −30 to −50 Pa. The appearing differences in pressure between the wind box spaces, the under-stoker space, and the atmosphere cause flows of uncontrolled leakages of air streams through the gaps existing between these spacer, however prober manufacturing of a boiler does not ensure its complete tightness. Sealing of the said spaces in a stoker-fired boiler, meaning the elimination of uncontrolled leakages of air not taking part in the solid fuel combustion process, was subject of many solutions and attempts. From the Polish patent No. 183654 description, it is known that a stoker-fired boiler burner has already been sealed by means of metallic membrane walls. Migration of air streams within a stoker-fired boiler may also be controlled through the appropriate shaping of wind boxes of the under-stoker wind boxes system. An example of a solution for the construction of an under-stoker wind boxes system, reducing the coefficient of excess air, was revealed in Polish patent application number P-355555.
  • DISCLOSURE OF INVENTION
  • The purpose of the invention was to reduce uncontrolled flows of air streams within a stoker-fired boiler, negatively affecting its performance.
  • A boiler according to the invention contains an combustion chamber with a secondary air channel, a movable mechanical stoker, and an under-stoker space containing an under-stoker wind boxes system with wind boxes, as well as a channel supplying the air into the inside of the wind boxes The essence of the invention is that the boiler contains an additional air channel with an inbuilt fan with adjustable output. One end of this additional air channel is connected with the under-stoker space located outside of the wind boxes of the under-stoker wind boxes system.
  • In other embodiments of the boiler according to the invention, the other end of the additional air channel is connected with either the space of the channel supplying the external air to the wind boxes of the under-stoker wind boxes system, or with the atmosphere or with the secondary air channel of the combustion chamber.
  • In another embodiment of the boiler according to the invention, in the space of the channel supplying the air from the atmosphere to the inside of the wind boxes as well as in the space of the additional air channel is located at least one air temperature sensor. These sensors may be connected to controller of the fan of the additional air channel.
  • A method of modernization according to the invention consists in that the under-stoker space of the aforementioned boiler, located outside of the wind boxes of the under-stoker wind boxes system, is connected with the first end of the additional air channel having an inbuilt fan with adjustable output.
  • In other embodiments of the method of modernization, the other end of the additional air channel is connected with either the space of the channel supplying the air to the wind boxes of the under-stoker wind boxes system, or with the atmosphere or with the secondary air channel of the combustion chamber.
  • In another embodiment of the the method of modernization, in the space of the channel supplying the air from the atmosphere to the inside of the wind boxes, as well as in the space of the additional air channel is located at least one air temperature sensor. These sensors may be connected to the controller of the fan of the additional air channel.
  • The method of elimination of uncontrolled air leakages according to the invention consists in leading out and air from the under-stoker space of a boiler, located outside of the wind boxes of the under-stoker wind boxes system, to an additional air channel having an inbuilt fan with changeable output. Current output of this fan is proportional to the current difference between temperature of air supplied to the wind boxes, and the temperature of air in the additional air channel.
  • In other embodiments of the method of elimination of uncontrolled air leakages, the air led out to the additional air channel is either supplied to the wind boxes of the under-stoker wind boxes system, or is led out further into the atmosphere, or supplied to the secondary air channel of the combustion chamber of the boiler.
  • The invention reduces the amount of air coming through the gaps and combining with the combustion fumes, giving in consequence a reduced coefficient of excess air in the fumes. This results in a reduction of a physical loss in the fumes, which also means the increase of boiler performance, usually by about 2 to 5%, depending on its technical condition, changes of the load, quality of the combustion charge, and proper maintenance and operation. The application of the invention also reduces the consumption of electric power by the components of the boiler by approximately 10-20%. As a result of general reduction of the amount of fumes removed from the boiler, the load of the extractor fan is smaller, and the consumption of energy by the fan of the additional air channel is balanced by limited energy consumption by the wind boxes air fan. A beneficial feature of the invention is also a short time needed for the modernization of the boiler, and a low cost of such modernization that amounts to ca. 10% of the cost of replacement of the under-stoker wind boxes system.
  • It unexpectedly appeared that a basic advantage of the invention is significant reduction of dust emission (20-70%), which gives hope for the possibility of meeting the requirements of future emission standards without installation of expensive electrostatic dust removers (dedusters). It also unexpectedly appeared that in the operation of the boiler with the invention being employed, emission of carbon oxide (CO) is reduced by 40-80%. This makes it possible not to equip boilers with secondary air fans, and reduces consumption of electricity.
  • BRIEF DESCRIPTION OF DRAWINGS
  • The invention has been shown in a drawing, presenting schematic vertical cross sections of a stoker-fired boiler, whereas
  • FIG. 1 presents a boiler with the first variant of an additional air channel,
  • FIG. 2 presents a boiler with the second variant of this channel, and
  • FIG. 3 presents a boiler with the third variant of such a channel.
  • MODE FOR CARRYING OUT THE INVENTION
  • A typical stoker-fired boiler has a fume zone with a fume extractor fan 1, and a burner zone. In the burner zone there is an combustion chamber 2, a movable mechanical stoker 3, an under-stoker wind boxes system 4 with wind boxes 5, and a channel 6 supplying the air from the atmosphere to the inside of the wind boxes 5 by means of a wind boxes air fan 7. The combustion chamber 2 has a secondary air channel powered by a fan 8. The boiler according to the invention has an additional air channel 9 with an inbuilt fan 10 with adjustable output. One end 9′ of the additional air channel 9 is connected with the under-stoker space 11 located outside of the wind boxes 5 of the under-stoker wind boxes system 4. The other end 9″ of the additional air channel 9 may be connected with either the space of channel 6 supplying external air to the wind boxes 5 of the under-stoker wind boxes system 4, or with the atmosphere or with the secondary air channel of the combustion chamber 2. Through controlling the output of the fan 10, an appropriate amount of air deriving from uncontrolled leakages is removed from the under-stoker zone 11, and directed to a selected place via the additional air channel 9. Output of the fan 10 may be controlled manually, whereas it is beneficial to use for this purpose the knowledge of air temperature in the space of channel 6 supplying it from the atmosphere to the inside of the wind boxes 5, and temperature of the air in the space of the additional air channel 9. In order to do so, in these places at least one air temperature sensor (not shown in the drawings) should be placed. For typical stoker-powered boilers, the difference between the temperature of wind boxes air stream in the channel 6, and temperature of air stream in the additional air channel 9 not exceeding 5° C. shows that through channel 9 flows only the air coming from uncontrolled leakages to the under-stoker space. The difference in temperatures amounting to 5 to 10° C. constitutes information that in the additional air channel 9 there also is the air deriving from uncontrolled leakages taking place through the section of the stoker 3 on which the combustion process no longer takes place or takes place into a limited extent. In this case, uncontrolled leakages take place towards the bottom part of the combustion chamber 2, and their reception has positive effects on the physical loss in the fumes. The difference in temperature exceeding 10° C. constitutes information that into the channel 9 additionally flow some of the fumes from the combustion chamber 2 without resulting in a physical loss in the fumes. These dependencies allow for automation of the adjustment of output of the fan 10, through connecting of the said temperature sensors to the fan controller, and the application of the difference between the temperatures measured by means of these sensors as a control parameter. It unexpectedly appeared that with small loads of the boiler, amounting to for instance 10-20% of the nominal load, the amount of air coming from the gaps is sufficient to conduct the process of combustion. In such a situation, when there is no possibility to isolate the channel 6 from the atmosphere, the wind boxes air fan 7 stops supplying air for the combustion process and only starts to block, the out-flow of air from the boiler. Elimination of air coming through the gaps from the stream of fumes in most cases causes the situation that the natural pull of the chimney suffices to ensure the appropriate negative pressure in the combustion chamber 2, causing purposelessness of operation of the fumes extractor fan 1. However, according to the mandatory regulations, boiler operation without an extractor fan 1 is not permitted. A solution to this problem may be operation with lower pressure value (e.g. −50 to −80 Pa in the combustion chamber 2), and limitation of output of the extractor fan 1. Very important for proper utilization of the boiler appeared to be the point of connection of the space of the channel 6 supplying wind boxes air with the space of the additional air channel 9. Connection at the point which causes the situation that most of the air supplied by the fan 10 reaches the front wind boxes 5 is unbeneficial for functioning of the boiler, particularly with the aforesaid temperature difference exceeding 10° C., because this means that an additional stream of air is supplied with a lower oxygen content. The same stream of air directed to the last operating wind boxes 5 positively affects the parameters of boiler operation, also with the temperature difference exceeding 10° C. This is connected with low intensity of the combustion process in this part of the stoker, meaning at the same time lower demand for oxygen. It unexpectedly appeared that connecting of the under-stoker space 11 through an additional air channel 9 with the atmosphere does not require changes of the insofar applied operation of the boiler (manual or automated). With the under-stoker space 11 connected with the channel 6 or the secondary air channel of the combustion chamber 2, the mutual interaction of the streams of air, in particular with the temperature difference exceeding 5° C., changes the insofar existing course of the combustion process, causing the need for measuring the streams of air and changing the boiler control algorithms. However, economic and ecological benefits resulting from lower electricity consumption, and the use of heat of the stream of air from the gaps, justify additional outlays incurred on the implementation of this solution, instead of a simpler to control connection of the under-stoker space 11 with the atmosphere. It also unexpectedly appeared that the application of the invention gives additional operation benefits. Connecting of the first wind box separated from the stream of wind boxes air with the under-stoker space allows boiler operators to control the distance of the point of coal ignition on the stoker from the slide gate and the front part of the boiler structure. Similarly, connecting of the last non-operating wind boxes with the under-stoker space after prior separation from the stream of wind boxes air reduces uncontrolled leakages from the wind boxes space to the combustion chamber.
  • According to the invention, it is possible to build new boilers, as well as quickly, cheaply and effectively modernize the existing ones. For example, modernization of a popular boiler type WR-10 entails installation of an additional air channel 9 with a centrifugal fan type WWOax-50 (made by Owent Olkusz) equipped with a 5.5 kW motor, whose rotation speed is controlled by means of a frequency converter. With manual control of this fan, decrease of stream of air supplied to the boiler was obtained by 6000 m3/h on average, with the boiler load within 30 to 80%. The application of both fans type WWOax-50 for modernization of a double-stoker boiler type WR-25 with the same manner of control of the fans caused a situation that within the load range of 40 to 80%, the excess air coefficient in the fumes dropped from the level of 2.0-2.5 to approximately 1.4-1.7. Temperature of combustion fumes after the boiler was reduced by 15 to 20° C., dust content in theses fumes stream was reduced by 20 to 70% and content of carbon oxide (CO) was reduced by 40-80%.

Claims (16)

1. A stoker-fired boiler having a combustion chamber (2) with a secondary air channel, movable mechanical stoker (3), and the under-stoker space (11) containing an under-stoker wind boxes system (4) with wind boxes (5), as well as a channel (6) supplying the air from the atmosphere to the inside of the wind boxes (5), characterized in that it contains an additional air channel (9) with an inbuilt fan (10) with adjustable output, wherein the first end (9′) of the additional air channel (9) is connected with the under-stoker space (11) located outside of the wind boxes (5) of the under-stoker wind boxes system (4).
2. The boiler according to claim 1, characterized in that the other end (9″) of the additional air channel (9) is connected with the space of the channel (6) supplying outside air to the wind boxes (5) of the under-stoker wind boxes system (4).
3. The boiler according to claim 1, characterized in that the other end (9″) of the additional air channel (9) is connected with the atmosphere.
4. The boiler according to claim 1, characterized in that the other end (9″) of the additional air channel (9) is connected with the secondary air channel of the combustion chamber (2).
5. The boiler according to any one of claims 1 to 4, characterized in that in the space of the channel (6) supplying the air from the atmosphere to the inside of the wind boxes (5) as well as in the space of the additional air channel (9) is located at least one air temperature sensor.
6. The boiler according to claim 5, characterized in that the air temperature sensors are connected to controller of the fan (10) of the additional air channel (9).
7. A method of modernization of a stoker-fire boiler containing a combustion chamber (2) with a secondary air channel, a movable mechanical stoker (3), and an under-stoker space (11) containing an under-stoker wind boxes system (4) with wind boxes (5), as well as a channel (6) supplying the air from the atmosphere to the inside of the wind boxes (5), characterized in that the under-stoker space (11) located outside of the wind boxes (5) of the under-stoker wind boxes system (4) is connected with the first end (9′) of the additional air channel (9) having an inbuilt fan (10) with adjustable output.
8. The method of modernization of a boiler according to claim 7, characterized in that the other end (9″) of the additional air channel (9) is connected with the space of the channel (6) supplying the outside air to the wind boxes (5) of the under-stoker wind boxes system (4).
9. The method of modernization of a boiler according to claim 7, characterized in that the other end (9″) of the additional air channel (9) is connected with the atmosphere.
10. The method of modernization of a boiler according to claim 7, characterized in that the other end (9″) of the additional air channel (9) is connected with the secondary air channel of the combustion chamber (2).
11. The method of modernization of a boiler according to any one of claims 7 to 10, characterized in that in the space of the channel (6) supplying the air from the atmosphere to the inside of the wind boxes (5) as well as in the space of the additional air channel (9) is located at least one air temperature sensor.
12. The method of modernization of a boiler according to claim 11, characterized in that the air temperature sensors are connected with controller of the fan (10) of the additional air channel (9).
13. A method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler containing a combustion chamber (2), movable mechanical stoker (3), and the under-stoker space (11) containing an under-stoker wind boxes system (4) with wind boxes (5), as well as a channel (6) supplying the air from the atmosphere to the inside of the wind boxes (5), characterized in that the air is led out from the under-stoker space (11) located outside of the wind boxes (5) of the under-stoker wind boxes system (4) to the additional air channel (9) with an inbuilt fan (10) with adjustable output, wherein current output of this fan (10) is proportional to the current difference between temperature of air supplied to the wind boxes (5) and temperature of air in the additional air channel (9).
14. The method of elimination of uncontrolled leakages according to claim 13, characterized in that the air led out to the additional air channel (9) is supplied to the wind boxes (5) of the under-stoker wind boxes system (4).
15. The method of elimination of uncontrolled leakages according to claim 13, characterized in that the air led out to the additional air channel (9) is led out further to the atmosphere.
16. The method of elimination of uncontrolled leakages according to claim 13, characterized in that the air led out to the additional air channel (9) is supplied to the secondary air channel of the combustion chamber (2).
US12/734,889 2007-12-03 2008-12-01 Stoker-fired boiler, a method of modernization of stoker-fired boilers and a method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler Abandoned US20100307393A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
PLP383941 2007-12-03
PL383941A PL383941A1 (en) 2007-12-03 2007-12-03 Stoker-fired boiler, the manner of modernization of a stoker-fired boiler and liquidation of harmful blow of air, which does not participate in combustion process in a stoker-fired boiler
PCT/PL2008/000092 WO2009072909A2 (en) 2007-12-03 2008-12-01 Stoker-fired boiler, a method of modernization of stoker-fired boilers and a method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler

Publications (1)

Publication Number Publication Date
US20100307393A1 true US20100307393A1 (en) 2010-12-09

Family

ID=40718395

Family Applications (1)

Application Number Title Priority Date Filing Date
US12/734,889 Abandoned US20100307393A1 (en) 2007-12-03 2008-12-01 Stoker-fired boiler, a method of modernization of stoker-fired boilers and a method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler

Country Status (10)

Country Link
US (1) US20100307393A1 (en)
EP (2) EP2461098A3 (en)
CN (1) CN101896771A (en)
AT (1) ATE552463T1 (en)
AU (1) AU2008332014A1 (en)
CA (1) CA2705730A1 (en)
PL (2) PL383941A1 (en)
RU (1) RU2447371C2 (en)
UA (1) UA94868C2 (en)
WO (1) WO2009072909A2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010052404A1 (en) * 2010-11-24 2012-05-24 Clyde Bergemann Drycon Gmbh Method and device for controlling combustion in a combustion boiler
CN104930697A (en) * 2014-03-18 2015-09-23 凤城市百利锅炉制造有限公司 Horizontal boiler
CN107448970A (en) * 2017-08-14 2017-12-08 山东天力节能环保工程有限公司 Boiler room
CN113803738A (en) * 2021-09-30 2021-12-17 鄂尔多斯市昊华国泰化工有限公司 Low-nitrogen combustion boiler with built-in tuyere circulation structure and method

Citations (63)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1324884A (en) * 1919-12-16 Jyubnace
US1614237A (en) * 1925-04-09 1927-01-11 Arthur E Grunert Furnace construction
US2381223A (en) * 1941-07-22 1945-08-07 Ind Engineering Corp Automatic control for heating systems
US2448891A (en) * 1943-11-20 1948-09-07 Harry P Katz Forced-draft air supply and control means for furnaces
US3174530A (en) * 1961-09-19 1965-03-23 Cyril F Meenan Furnace combustion chamber
US3898317A (en) * 1972-07-24 1975-08-05 Midland Ross Corp Method for incinerating flue gases
US3955909A (en) * 1971-11-15 1976-05-11 Aqua-Chem, Inc. Reduction of gaseous pollutants in combustion flue gas
US4036576A (en) * 1976-08-11 1977-07-19 The Trane Company Incineration system for the disposal of a waste gas and method of operation
US4113417A (en) * 1974-11-06 1978-09-12 Stein Industrie Combustion of hot gases of low calorific power
US4263857A (en) * 1979-01-05 1981-04-28 Dravo Corporation Traveling grate stoker for the combustion of difficultly ignited fuels
US4340355A (en) * 1980-05-05 1982-07-20 Honeywell Inc. Furnace control using induced draft blower, exhaust gas flow rate sensing and density compensation
US4362269A (en) * 1981-03-12 1982-12-07 Measurex Corporation Control system for a boiler and method therefor
US4375950A (en) * 1981-04-01 1983-03-08 Durley Iii Benton A Automatic combustion control method and apparatus
US4381988A (en) * 1981-07-20 1983-05-03 Dravo Corporation Fine particulate removal from oil shale on a travelling grate retort
US4446800A (en) * 1981-03-10 1984-05-08 Hb Megaron Apparatus for firing solid fuels
US4588372A (en) * 1982-09-23 1986-05-13 Honeywell Inc. Flame ionization control of a partially premixed gas burner with regulated secondary air
US4628838A (en) * 1980-11-19 1986-12-16 Peabody Engineering Corp. Fluidized bed combustion method
US4648329A (en) * 1983-11-09 1987-03-10 Manutair Moller Device for reinjecting flown-off particles into a solid fuel boiler
US4697530A (en) * 1986-12-23 1987-10-06 Dumont Holding Company Underfed stoker boiler for burning bituminous coal and other solid fuel particles
US4838183A (en) * 1988-02-11 1989-06-13 Morse Boulger, Inc. Apparatus and method for incinerating heterogeneous materials
US4905613A (en) * 1988-09-09 1990-03-06 Detroit Stoker Company Fuel feeder
US5031549A (en) * 1990-10-04 1991-07-16 Westinghouse Electric Corp. Method of introducing air into a rotary combustor
US5044288A (en) * 1988-12-01 1991-09-03 Barlow James L Method and apparatus for the efficient combustion of a mass fuel
US5230293A (en) * 1991-02-22 1993-07-27 Von Roll Ag Method and apparatus for controlling a refuse incineration plant
US5241916A (en) * 1991-02-07 1993-09-07 Martin Gmbh Fur Umwelt- Und Energietechnik Procedure for supplying combustion air and a furnace therefor
US5261337A (en) * 1991-06-21 1993-11-16 Mitsubishi Jukogyo Kabushiki Kaisha Combustion control method of refuse incinerator
US5307746A (en) * 1990-02-28 1994-05-03 Institute Of Gas Technology Process and apparatus for emissions reduction from waste incineration
US5357879A (en) * 1992-05-20 1994-10-25 Ebara-Infilco Co., Ltd. Dried sludge melting furnace
US5359967A (en) * 1993-06-15 1994-11-01 Carter Hudson R Combined thermal and fuel NOx control utilizing furnace cleanliness and stoichiometric burner combustion
US5484476A (en) * 1994-01-11 1996-01-16 Electric Power Research Institute, Inc. Method for preheating fly ash
US5496450A (en) * 1994-04-13 1996-03-05 Blumenthal; Robert N. Multiple on-line sensor systems and methods
US5588378A (en) * 1995-04-18 1996-12-31 New York State Electric & Gas Corporation Combustion enhancement system with in-bed foils
US5601071A (en) * 1995-01-26 1997-02-11 Tridelta Industries, Inc. Flow control system
US5606924A (en) * 1993-12-29 1997-03-04 Martin Gmbh Fuer Umwelt- Und Energietechnik Process for regulating individual factors or all factors influencing combustion on a furnace grate
US5634412A (en) * 1994-08-09 1997-06-03 Martin Gmbh Fuer Umwelt- Und Energietechnik Method for regulating the furnace in incineration plants in particular in refuse incineration plants
US5806440A (en) * 1995-06-09 1998-09-15 Texas Instruments Incorporated Method for controlling an induced draft fan for use with gas furnaces
US5813767A (en) * 1995-09-29 1998-09-29 Finmeccanica S.P.A. Azienda Ansaldo System and a method for monitoring combustion and pollutants in a thermal plant by means of laser diodes
US6019593A (en) * 1998-10-28 2000-02-01 Glasstech, Inc. Integrated gas burner assembly
US6085674A (en) * 1999-02-03 2000-07-11 Clearstack Combustion Corp. Low nitrogen oxides emissions from carbonaceous fuel combustion using three stages of oxidation
US6145453A (en) * 1998-05-05 2000-11-14 Martin Gmbh Fuer Unwelt- Und Energietechnik Method for controlling the firing rate of combustion installations
US6155183A (en) * 1996-01-31 2000-12-05 A E P Resources Service Company Method and apparatus for reducing NOx emissions from a multiple-intertube pulverized-coal burner
US6289266B1 (en) * 1999-05-14 2001-09-11 Allegheny Power Service Corporation Method of operating a boiler
US6537059B2 (en) * 2000-05-12 2003-03-25 Siemens Building Technologies Ag Regulating device for a burner
US6638061B1 (en) * 2002-08-13 2003-10-28 North American Manufacturing Company Low NOx combustion method and apparatus
US6655304B1 (en) * 1999-05-21 2003-12-02 Barlow Projects, Inc. Mass fuel combustion system
US6705533B2 (en) * 2001-04-20 2004-03-16 Gas Research Institute Digital modulation for a gas-fired heater
US6764298B2 (en) * 2001-04-16 2004-07-20 Lg Electronics Inc. Method for controlling air fuel ratio in gas furnace
US20040191914A1 (en) * 2003-03-28 2004-09-30 Widmer Neil Colin Combustion optimization for fossil fuel fired boilers
US6799526B2 (en) * 1997-09-26 2004-10-05 American Air Liquide, Inc. Methods of improving productivity of black liquor recovery boilers
US20040244367A1 (en) * 2003-06-05 2004-12-09 Swanson Larry William Multi-compartment overfire air and N-agent injection system and method for nitrogen oxide reduction in flue gas
US20040255831A1 (en) * 2003-06-18 2004-12-23 Joseph Rabovitser Combustion-based emission reduction method and system
US6866202B2 (en) * 2001-09-10 2005-03-15 Varidigm Corporation Variable output heating and cooling control
US7347112B2 (en) * 2004-05-03 2008-03-25 Environemental Monitoring Systems, Inc. Air sampler with integrated airflow sensing
US7401577B2 (en) * 2003-03-19 2008-07-22 American Air Liquide, Inc. Real time optimization and control of oxygen enhanced boilers
US7497172B2 (en) * 2005-10-12 2009-03-03 Breen Energy Solutions Method to decrease emissions of nitrogen oxides and mercury through in-situ gasification of carbon/water slurries
US20100112500A1 (en) * 2008-11-03 2010-05-06 Maiello Dennis R Apparatus and method for a modulating burner controller
US7756591B2 (en) * 2006-04-25 2010-07-13 Pegasus Technologies, Inc. System for optimizing oxygen in a boiler
US20100206203A1 (en) * 2007-05-21 2010-08-19 Mario Magaldi System for dry extracting/cooling heterogeneous material ashes with control of the air inlet in the combustion chamber
US7802984B2 (en) * 2006-04-07 2010-09-28 Thomas & Betts International, Inc. System and method for combustion-air modulation of a gas-fired heating system
US7832342B2 (en) * 2005-03-04 2010-11-16 Martin GmbH für Umwelt-und Energietechnik Process for combusting fuels, in particular waste
US7975628B2 (en) * 2006-09-13 2011-07-12 Martin GmbH für Umwelt- und Energietechnik Method for supplying combustion gas in incineration systems
US20110232544A1 (en) * 2008-12-12 2011-09-29 Foster Wheeler Energia Oy Oxycombustion Circulating Fluidized Bed Reactor, Method of Operating Such a Reactor and Method of Upgrading a Circulating Fluidized Bed Reactor
US8196532B2 (en) * 2008-02-27 2012-06-12 Andrus Jr Herbert E Air-fired CO2 capture ready circulating fluidized bed heat generation with a reactor subsystem

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE394358A (en) *
GB973244A (en) 1960-02-05 1964-10-21 Ivor John Conibear Improvements in furnaces fitted with chain grate stokers
RU2078283C1 (en) * 1995-03-07 1997-04-27 Челябинская ТЭЦ-2 Method and device for burning ground coal
RU2244873C2 (en) * 2002-07-29 2005-01-20 Туманов Сергей Сергеевич Furnace for burning wood wastes in fluidized bed
RU2294483C1 (en) * 2005-08-17 2007-02-27 Сергей Алексеевич Концевой Method and device for burning solid fuel

Patent Citations (65)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1324884A (en) * 1919-12-16 Jyubnace
US1614237A (en) * 1925-04-09 1927-01-11 Arthur E Grunert Furnace construction
US2381223A (en) * 1941-07-22 1945-08-07 Ind Engineering Corp Automatic control for heating systems
US2448891A (en) * 1943-11-20 1948-09-07 Harry P Katz Forced-draft air supply and control means for furnaces
US3174530A (en) * 1961-09-19 1965-03-23 Cyril F Meenan Furnace combustion chamber
US3955909A (en) * 1971-11-15 1976-05-11 Aqua-Chem, Inc. Reduction of gaseous pollutants in combustion flue gas
US3898317A (en) * 1972-07-24 1975-08-05 Midland Ross Corp Method for incinerating flue gases
US4113417A (en) * 1974-11-06 1978-09-12 Stein Industrie Combustion of hot gases of low calorific power
US4036576A (en) * 1976-08-11 1977-07-19 The Trane Company Incineration system for the disposal of a waste gas and method of operation
US4263857A (en) * 1979-01-05 1981-04-28 Dravo Corporation Traveling grate stoker for the combustion of difficultly ignited fuels
US4340355A (en) * 1980-05-05 1982-07-20 Honeywell Inc. Furnace control using induced draft blower, exhaust gas flow rate sensing and density compensation
US4628838A (en) * 1980-11-19 1986-12-16 Peabody Engineering Corp. Fluidized bed combustion method
US4446800A (en) * 1981-03-10 1984-05-08 Hb Megaron Apparatus for firing solid fuels
US4362269A (en) * 1981-03-12 1982-12-07 Measurex Corporation Control system for a boiler and method therefor
US4375950A (en) * 1981-04-01 1983-03-08 Durley Iii Benton A Automatic combustion control method and apparatus
US4381988A (en) * 1981-07-20 1983-05-03 Dravo Corporation Fine particulate removal from oil shale on a travelling grate retort
US4588372A (en) * 1982-09-23 1986-05-13 Honeywell Inc. Flame ionization control of a partially premixed gas burner with regulated secondary air
US4648329A (en) * 1983-11-09 1987-03-10 Manutair Moller Device for reinjecting flown-off particles into a solid fuel boiler
US4739715A (en) * 1983-11-09 1988-04-26 Couarc H Michel F E Process and device for reinjecting flown-off particles into a solid fuel boiler
US4697530A (en) * 1986-12-23 1987-10-06 Dumont Holding Company Underfed stoker boiler for burning bituminous coal and other solid fuel particles
US4838183A (en) * 1988-02-11 1989-06-13 Morse Boulger, Inc. Apparatus and method for incinerating heterogeneous materials
US4905613A (en) * 1988-09-09 1990-03-06 Detroit Stoker Company Fuel feeder
US5044288A (en) * 1988-12-01 1991-09-03 Barlow James L Method and apparatus for the efficient combustion of a mass fuel
US5307746A (en) * 1990-02-28 1994-05-03 Institute Of Gas Technology Process and apparatus for emissions reduction from waste incineration
US5031549A (en) * 1990-10-04 1991-07-16 Westinghouse Electric Corp. Method of introducing air into a rotary combustor
US5241916A (en) * 1991-02-07 1993-09-07 Martin Gmbh Fur Umwelt- Und Energietechnik Procedure for supplying combustion air and a furnace therefor
US5230293A (en) * 1991-02-22 1993-07-27 Von Roll Ag Method and apparatus for controlling a refuse incineration plant
US5261337A (en) * 1991-06-21 1993-11-16 Mitsubishi Jukogyo Kabushiki Kaisha Combustion control method of refuse incinerator
US5357879A (en) * 1992-05-20 1994-10-25 Ebara-Infilco Co., Ltd. Dried sludge melting furnace
US5359967A (en) * 1993-06-15 1994-11-01 Carter Hudson R Combined thermal and fuel NOx control utilizing furnace cleanliness and stoichiometric burner combustion
US5606924A (en) * 1993-12-29 1997-03-04 Martin Gmbh Fuer Umwelt- Und Energietechnik Process for regulating individual factors or all factors influencing combustion on a furnace grate
US5484476A (en) * 1994-01-11 1996-01-16 Electric Power Research Institute, Inc. Method for preheating fly ash
US5496450A (en) * 1994-04-13 1996-03-05 Blumenthal; Robert N. Multiple on-line sensor systems and methods
US5634412A (en) * 1994-08-09 1997-06-03 Martin Gmbh Fuer Umwelt- Und Energietechnik Method for regulating the furnace in incineration plants in particular in refuse incineration plants
US5601071A (en) * 1995-01-26 1997-02-11 Tridelta Industries, Inc. Flow control system
US5588378A (en) * 1995-04-18 1996-12-31 New York State Electric & Gas Corporation Combustion enhancement system with in-bed foils
US5806440A (en) * 1995-06-09 1998-09-15 Texas Instruments Incorporated Method for controlling an induced draft fan for use with gas furnaces
US5813767A (en) * 1995-09-29 1998-09-29 Finmeccanica S.P.A. Azienda Ansaldo System and a method for monitoring combustion and pollutants in a thermal plant by means of laser diodes
US6155183A (en) * 1996-01-31 2000-12-05 A E P Resources Service Company Method and apparatus for reducing NOx emissions from a multiple-intertube pulverized-coal burner
US6799526B2 (en) * 1997-09-26 2004-10-05 American Air Liquide, Inc. Methods of improving productivity of black liquor recovery boilers
US6145453A (en) * 1998-05-05 2000-11-14 Martin Gmbh Fuer Unwelt- Und Energietechnik Method for controlling the firing rate of combustion installations
US6019593A (en) * 1998-10-28 2000-02-01 Glasstech, Inc. Integrated gas burner assembly
US6085674A (en) * 1999-02-03 2000-07-11 Clearstack Combustion Corp. Low nitrogen oxides emissions from carbonaceous fuel combustion using three stages of oxidation
US6289266B1 (en) * 1999-05-14 2001-09-11 Allegheny Power Service Corporation Method of operating a boiler
US6655304B1 (en) * 1999-05-21 2003-12-02 Barlow Projects, Inc. Mass fuel combustion system
US6537059B2 (en) * 2000-05-12 2003-03-25 Siemens Building Technologies Ag Regulating device for a burner
US6764298B2 (en) * 2001-04-16 2004-07-20 Lg Electronics Inc. Method for controlling air fuel ratio in gas furnace
US6705533B2 (en) * 2001-04-20 2004-03-16 Gas Research Institute Digital modulation for a gas-fired heater
US6866202B2 (en) * 2001-09-10 2005-03-15 Varidigm Corporation Variable output heating and cooling control
US6638061B1 (en) * 2002-08-13 2003-10-28 North American Manufacturing Company Low NOx combustion method and apparatus
US7401577B2 (en) * 2003-03-19 2008-07-22 American Air Liquide, Inc. Real time optimization and control of oxygen enhanced boilers
US20040191914A1 (en) * 2003-03-28 2004-09-30 Widmer Neil Colin Combustion optimization for fossil fuel fired boilers
US7838297B2 (en) * 2003-03-28 2010-11-23 General Electric Company Combustion optimization for fossil fuel fired boilers
US20040244367A1 (en) * 2003-06-05 2004-12-09 Swanson Larry William Multi-compartment overfire air and N-agent injection system and method for nitrogen oxide reduction in flue gas
US20040255831A1 (en) * 2003-06-18 2004-12-23 Joseph Rabovitser Combustion-based emission reduction method and system
US7347112B2 (en) * 2004-05-03 2008-03-25 Environemental Monitoring Systems, Inc. Air sampler with integrated airflow sensing
US7832342B2 (en) * 2005-03-04 2010-11-16 Martin GmbH für Umwelt-und Energietechnik Process for combusting fuels, in particular waste
US7497172B2 (en) * 2005-10-12 2009-03-03 Breen Energy Solutions Method to decrease emissions of nitrogen oxides and mercury through in-situ gasification of carbon/water slurries
US7802984B2 (en) * 2006-04-07 2010-09-28 Thomas & Betts International, Inc. System and method for combustion-air modulation of a gas-fired heating system
US7756591B2 (en) * 2006-04-25 2010-07-13 Pegasus Technologies, Inc. System for optimizing oxygen in a boiler
US7975628B2 (en) * 2006-09-13 2011-07-12 Martin GmbH für Umwelt- und Energietechnik Method for supplying combustion gas in incineration systems
US20100206203A1 (en) * 2007-05-21 2010-08-19 Mario Magaldi System for dry extracting/cooling heterogeneous material ashes with control of the air inlet in the combustion chamber
US8196532B2 (en) * 2008-02-27 2012-06-12 Andrus Jr Herbert E Air-fired CO2 capture ready circulating fluidized bed heat generation with a reactor subsystem
US20100112500A1 (en) * 2008-11-03 2010-05-06 Maiello Dennis R Apparatus and method for a modulating burner controller
US20110232544A1 (en) * 2008-12-12 2011-09-29 Foster Wheeler Energia Oy Oxycombustion Circulating Fluidized Bed Reactor, Method of Operating Such a Reactor and Method of Upgrading a Circulating Fluidized Bed Reactor

Also Published As

Publication number Publication date
PL2217858T3 (en) 2012-09-28
EP2217858A2 (en) 2010-08-18
PL383941A1 (en) 2009-06-08
EP2217858B1 (en) 2012-04-04
ATE552463T1 (en) 2012-04-15
UA94868C2 (en) 2011-06-10
AU2008332014A1 (en) 2009-06-11
WO2009072909A3 (en) 2009-08-06
CN101896771A (en) 2010-11-24
RU2447371C2 (en) 2012-04-10
CA2705730A1 (en) 2009-06-11
EP2461098A3 (en) 2014-08-27
EP2461098A2 (en) 2012-06-06
RU2010126547A (en) 2012-01-10
WO2009072909A2 (en) 2009-06-11
WO2009072909A4 (en) 2009-10-15

Similar Documents

Publication Publication Date Title
US20100307393A1 (en) Stoker-fired boiler, a method of modernization of stoker-fired boilers and a method of elimination of uncontrolled leakages of air not taking part in the combustion process in a stoker-fired boiler
CN106766220A (en) A kind of gas water heater control system of air quantity self adaptation
CN104801416A (en) Control system and control method for outlet temperature of novel coal mill
CN106861407B (en) It is a kind of for avoiding the blower of paired running from tacking the control method of phenomenon
JP6333021B2 (en) Incineration processing equipment and incineration processing method
CN204830359U (en) Pressure differential control system of positive control room
CN208333130U (en) A kind of melting furnace smoke discharging pipe system
CN106403626A (en) Full-automatic starting system and method for sintering waste heat recycling and sintering draught fan combined unit
CN211291013U (en) Sintering machine with micro-negative pressure adjusting device
RU105714U1 (en) BOILER INSTALLATION
CN206359466U (en) A kind of coke oven flue suction equalization system
CN210532690U (en) Hot air system for production workshop
CN108758774A (en) Control method, control system and the gas furnace of gas furnace
CN102345975A (en) Cement production line material drying temperature control method and device adopting waste heat power generation
CN201306732Y (en) A bioler coal feeding and input air synchronization intelligence control system
CN205317007U (en) Independent fume extractor on roller of roller kilns, under roller
CN204513438U (en) A kind of boiler original coal bunker dehumidifying fluidization system
CN216972317U (en) Smoke exhaust system of glass melting furnace
CN102865747A (en) Smoke afterheat utilization system and smoke afterheat utilization method for electrical porcelain kiln group
CN102840585A (en) Three-driving inverse push type incinerator grate and feeding device control method, device and system
CN216049031U (en) Drying and ventilating system
CN104163581A (en) A sealing method for a lime sleeve kiln having an output of 500 t/d
CN210898227U (en) Distribution box with cooling function on gas collecting hood of resistance furnace
CN202644187U (en) Glass fiber desizing furnace heat control system
CN204325399U (en) Converter dedusting line

Legal Events

Date Code Title Description
STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION