CN106288370B - Gas boiler based on porous media combustion technology - Google Patents

Gas boiler based on porous media combustion technology Download PDF

Info

Publication number
CN106288370B
CN106288370B CN201610807386.6A CN201610807386A CN106288370B CN 106288370 B CN106288370 B CN 106288370B CN 201610807386 A CN201610807386 A CN 201610807386A CN 106288370 B CN106288370 B CN 106288370B
Authority
CN
China
Prior art keywords
combustion
chamber
heat exchange
water
outlet
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.)
Active
Application number
CN201610807386.6A
Other languages
Chinese (zh)
Other versions
CN106288370A (en
Inventor
王恩宇
沈家利
苟湘
吴晋湘
刘联胜
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.)
Hebei Hongtan Energy Technology Co Ltd
Original Assignee
Hebei University of Technology
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 Hebei University of Technology filed Critical Hebei University of Technology
Priority to CN201610807386.6A priority Critical patent/CN106288370B/en
Publication of CN106288370A publication Critical patent/CN106288370A/en
Application granted granted Critical
Publication of CN106288370B publication Critical patent/CN106288370B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/22Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
    • F24H1/44Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with combinations of two or more of the types covered by groups F24H1/24 - F24H1/40 , e.g. boilers having a combination of features covered by F24H1/24 - F24H1/40
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00Details
    • F24H9/0005Details for water heaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00Details
    • F24H9/18Arrangement or mounting of grates or heating means
    • F24H9/1809Arrangement or mounting of grates or heating means for water heaters
    • F24H9/1832Arrangement or mounting of combustion heating means, e.g. grates or burners
    • F24H9/1836Arrangement or mounting of combustion heating means, e.g. grates or burners using fluid fuel

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

本发明涉及基于多孔介质燃烧技术的燃气锅炉,包括预混器、若干数量的燃烧换热单元和连接箱体;所述若干数量的燃烧换热单元通过连接箱体连接,燃烧换热单元围绕连接箱体呈中心对称分布,连接箱体和燃烧换热单元外部包裹有外壳,在外壳与连接箱体和燃烧换热单元之间填充有保温材料,预混器设置在连接箱体的上部;所述燃烧换热单元包括防回火结构、燃烧室、尾部换热器和进气室,所述进气室的侧壁面焊接有两个预混气体进口管;所述防回火结构由防回火水室和防回火进气通道构成,防回火进气通道通过焊接嵌入在防回火水室中,防回火水室前端与进气室连接,在防回火水室后端连接燃烧室,在燃烧室的出口布置有尾部换热器。

Figure 201610807386

The invention relates to a gas boiler based on porous medium combustion technology, comprising a premixer, a number of combustion heat exchange units and a connection box; the number of combustion heat exchange units are connected through the connection box, and the combustion heat exchange units are connected around the connection The box body is symmetrically distributed in the center, the connection box body and the combustion heat exchange unit are wrapped with an outer shell, and the insulation material is filled between the outer shell and the connection box body and the combustion heat exchange unit, and the premixer is arranged on the upper part of the connection box body; The combustion heat exchange unit includes an anti-backfire structure, a combustion chamber, a rear heat exchanger and an intake chamber, and two premixed gas inlet pipes are welded on the side wall surface of the intake chamber; The fire water chamber and the anti-tempering air intake channel are formed. The anti-tempering air intake channel is embedded in the anti-tempering water chamber by welding. The combustion chamber is provided with a rear heat exchanger at the outlet of the combustion chamber.

Figure 201610807386

Description

Gas boiler based on porous medium combustion technology
Technical Field
The invention relates to the technical field of water heaters which surround a combustion chamber by a heat exchange water chamber and realize waste heat recovery by a heat exchange device, in particular to a gas boiler based on porous medium combustion technology.
Background
With the optimization and adjustment of energy structures in China, gas boilers are concerned about due to the characteristics of economy, high efficiency and environmental protection. But countries all over the world put higher demands on energy utilization efficiency and environmental pollutant emissionThe existing gas-fired boiler has low heat efficiency and high pollutant emission. In order to improve the efficiency of the boiler, the prior art is to increase the heat exchange area or add a waste heat recovery device, which makes the structure of the boiler more complicated and the volume larger. The existing gas-fired boiler almost adopts the traditional combustion mode, the temperature of the combustion area is higher, NO is generatedxThe discharge amount of (2) is large.
Disclosure of Invention
The technical problem to be solved by the invention is as follows: the utility model provides a gas boiler based on porous medium combustion technology, comprises a plurality of burning heat transfer units, adopts the furnace type structure of symmetrical arrangement. The combustion chamber in each combustion heat exchange unit is divided into a plurality of small areas by the heat exchange water chamber, and the combustion chamber is filled with non-uniform porous medium materials, so that the combustion and heat exchange characteristics of the porous medium are fully utilized, the heat exchange effect is ensured, the combustion temperature is limited, and the low NO is realizedxAnd (5) discharging. Overcomes the defects of large volume, low heat efficiency and NO generation caused by overhigh combustion temperature of the prior gas-fired boilerxHigh discharge. 2-12 combustion heat exchange units can be symmetrically arranged according to the capacity of the boiler, so that the gas boiler has higher load regulation capacity.
The technical scheme adopted by the invention for solving the technical problem is as follows:
the gas boiler based on the porous medium combustion technology comprises a premixer, a plurality of combustion heat exchange units and a connecting box body; the combustion heat exchange units are connected through the connecting box body, the combustion heat exchange units are distributed around the connecting box body in a central symmetry manner, the outer parts of the connecting box body and the combustion heat exchange units are wrapped by shells, heat insulation materials are filled among the shells, the connecting box body and the combustion heat exchange units, and the premixer is arranged at the upper part of the connecting box body;
the combustion heat exchange unit comprises an anti-backfire structure, a combustion chamber, a tail heat exchanger and an air inlet chamber, wherein two premixed gas inlet pipes are welded on the side wall surface of the air inlet chamber; the anti-backfire structure consists of an anti-backfire water chamber and an anti-backfire air inlet channel, the anti-backfire air inlet channel is embedded in the anti-backfire water chamber by welding, the front end of the anti-backfire water chamber is connected with the air inlet chamber, the rear end of the anti-backfire water chamber is connected with the combustion chamber, a tail heat exchanger is arranged at an outlet of the combustion chamber, the combustion chamber and the tail heat exchanger are both arranged in the combustion chamber inner shell, and the air inlet chamber and the combustion chamber are communicated through the anti-backfire air inlet channel; filling a small-pore porous medium material in the anti-backfire air inlet channel; a plurality of heat exchange water chambers are distributed in the inner shell of the combustion chamber at intervals, the combustion chamber is divided into a plurality of small combustion areas by the plurality of heat exchange water chambers, non-uniform porous medium materials are filled in the small combustion areas, and refractory bricks are arranged at the upper end and the lower end of each small combustion area and close to the inner shell of the combustion chamber; the number of rows of the anti-backfire air inlet channels is the same as the number of small areas of the combustion chamber; a gap is reserved at the upstream of the combustion chamber and the part connected with the anti-backfire water chamber, and an igniter electrode is fixedly arranged in the gap;
the anti-backfire water chamber is welded with an anti-backfire water chamber water inlet pipe and an anti-backfire water chamber water outlet pipe, the heat exchange water chamber is welded with a heat exchange water chamber water outlet pipe and a heat exchange water chamber water inlet pipe, two ends of the heat exchange water chamber water inlet pipe are sealed, an inlet and a plurality of outlets are arranged, the number of the outlets is consistent with that of the heat exchange water chamber, and each outlet is respectively communicated with one heat exchange water chamber; the outlet pipe of the anti-backfire water chamber is connected with the inlet of the inlet pipe of the heat exchange water chamber, and the outlets of a plurality of heat exchange water chambers of each combustion heat exchange unit are communicated with the outlet pipe of the heat exchange water chamber;
the tail heat exchanger comprises a tail heat exchange tube, a tail heat exchanger inlet header and a tail heat exchanger outlet header, two ends of the tail heat exchange tube are respectively welded on the tail heat exchanger inlet header and the tail heat exchanger outlet header, and the tail heat exchange tube is fixedly connected with the side wall of the combustion chamber inner shell; the outlet header of the tail heat exchanger is connected with the water inlet pipe of the backfire-proof water chamber through a connecting water pipe;
the connecting box body comprises a plurality of connecting box body side plates, a connecting box body top plate and a connecting box body bottom plate, the number of the connecting box body side plates is consistent with that of the combustion heat exchange units, a box body space defined by the connecting box body side plates, the connecting box body top plate and the connecting box body bottom plate forms a flue gas collecting chamber, each connecting box body side plate is welded with a side plate of a combustion chamber inner shell of the corresponding combustion heat exchange unit, and the connecting box body top plate and the connecting box body bottom plate are welded with a top plate and a bottom plate of the combustion chamber inner shell of the corresponding combustion heat exchange unit; the bottom of the connecting box body is of a reverse pyramid structure, a cylindrical condensate water collecting chamber is welded in the center of the bottom plate of the connecting box body, and a drain pipe and a smoke exhaust pipe are welded on the condensate water collecting chamber;
the bottom of the connecting box body is provided with an annular boiler inlet collecting pipe, a boiler water inlet pipe is welded on the boiler inlet collecting pipe, a plurality of water outlets with the same number as that of the combustion heat exchange units are arranged on the boiler inlet collecting pipe, the water outlets are connected with the tail heat exchanger inlet collecting pipe of the corresponding combustion heat exchange unit, and a plurality of water valves with the same number as that of the combustion heat exchange units are arranged on the annular boiler inlet collecting pipe; the top of the connecting box body is provided with an annular boiler outlet collecting pipe, the boiler outlet collecting pipe is provided with a plurality of water inlets and a water outlet, the number of the water inlets and the number of the water outlet are consistent with that of the combustion heat exchange units, the water inlets are respectively connected with the heat exchange water chambers of the corresponding combustion heat exchange units through water pipes, and the water outlets of the boiler outlet collecting pipe are welded with hot water outlet pipes.
Compared with the prior art, the invention has the beneficial effects that:
the invention has the following prominent essential characteristics: the invention adopts the non-uniform porous medium heat accumulation combustion technology, the combustion is more stable, the combustion intensity is high, the heat exchange effect is good, and the pollutant discharge is low. (1) The combustion chamber is divided into a plurality of small areas by the heat exchange water chamber, and the cold water medium and the heating medium are tightly attached, so that the combustion strength is ensured, and meanwhile, the combustion heat is quickly and efficiently transferred to the cold water medium, so that the combustion temperature in the combustion chamber is reduced; the method is that the combustion chamber is filled with heterogeneous porous medium material, and the heat in the high temperature porous medium is transferred to the cold water medium in the heat exchange water chamber in the forms of radiation and heat conduction. (2) A waste heat recovery area is arranged at the outlet of the combustion chamber, and sensible heat of high-temperature flue gas and latent heat of water vapor are collected; the method is that a tail heat exchanger is arranged at the rear end of the combustor, so that water vapor in high-temperature flue gas is condensed to release condensation heat. (3) The premixed gas passes through an air inlet channel of the tempering-preventing water chamber before entering the combustion chamber, and a small-pore porous medium material is filled in the air inlet channel to rectify the premixed gas, improve the flow rate of the premixed gas and prevent tempering; (4) the water in the heat exchange water chamber is preheated by the tail heat exchanger, so that the temperature of the wall surface of the combustion chamber is improved, the problem of condensate water caused by supercooling of the wall surface is reduced, the combustion condition of the wall surface is improved, and the combustion completeness is improved.
The invention has the remarkable advantages that:
(1) the porous medium material arrangement structure in the combustion chamber of the gas boiler based on the porous medium combustion technology is non-uniform, the flow resistance is small, the combustion is more stable, the combustion chamber is divided into a plurality of small areas by the heat exchange water chamber, the dispersed combustion is realized, the combustion temperature is effectively reduced, and the low NO is realizedxAnd (4) discharging.
(2) The gas boiler based on the porous medium combustion technology is of a central symmetrical structure and comprises 2-12 combustion heat exchange units, partial units can be controlled to work according to the requirement of heat load, and the gas boiler has higher load regulation capacity.
(3) The gas boiler based on the porous medium combustion technology is a condensing boiler, so that the heat released by combustion is absorbed to the maximum extent, and the defects of larger volume and lower heat efficiency of the boiler device in the prior art are overcome.
The invention utilizes the characteristic of enhanced heat exchange of the porous medium to reduce the flue gas to be very low in the combustion chamber, and simultaneously supplements a tail heat exchanger at the tail part of the combustion chamber to further reduce the temperature of the flue gas.
Drawings
The invention is further illustrated with reference to the following figures and examples.
FIG. 1 is a schematic sectional elevation view of a gas boiler based on porous medium combustion technology having 4 combustion heat exchange units according to the present invention;
FIG. 2 is a schematic sectional top view of a gas boiler based on porous medium combustion technology with 4 combustion heat exchange units according to the present invention;
FIG. 3 is a schematic cross-sectional view of the embodiment of FIG. 1 at a location A-A in accordance with the present invention of a gas boiler based on porous medium combustion technology;
FIG. 4 is a schematic cross-sectional view of the embodiment of FIG. 1 at a location B-B in accordance with the present invention of a gas boiler based on porous medium combustion technology;
fig. 5 is a schematic top sectional view of an embodiment of a gas boiler based on porous medium combustion technology with 6 combustion heat exchange units, connecting box bodies.
In the figure, 1, a premixed gas inlet pipe, 2, an air inlet chamber, 3, a heat insulation material, 4, a backfire-proof air inlet channel, 5, an outer shell, 6, a backfire-proof water chamber water inlet pipe, 7, a connecting water pipe, 8, a heat exchange water chamber water outlet pipe, 9, refractory bricks, 10, a tail heat exchanger outlet header, 11, a boiler outlet header, 12, a premixed gas communication pipe, 13, an ejector, 14, a premixing chamber, 15, a connecting box side plate, 16, a connecting box top plate, 17, a premixed gas outlet pipe, 18, a stop valve, 19, an air nozzle, 20, a gas nozzle, 21, a heat exchange water chamber water inlet pipe, 22, a boiler inlet header, 23, a water valve, 24, a tail heat exchanger inlet header, 25, a drain pipe, 26, a smoke exhaust pipe, 27, a condensate water collecting chamber, 28, a connecting box bottom plate, 29, a tail heat exchange pipe, 30, a positioning sheet, 31, a combustion chamber inner shell, 32 and an igniter electrode, 33. the water outlet pipe of the backfire preventing water chamber, 34, the non-uniform porous medium material, 35, the backfire preventing water chamber, 36, the small-pore porous medium material, 37, the boiler water inlet pipe, 38, the hot water outlet pipe, 39, the heat exchange water chamber and 40, the combustion chamber.
Detailed Description
The gas boiler (boiler for short, see figures 1-4) based on the porous medium combustion technology comprises a premixer, a plurality of combustion heat exchange units and a connecting box body; the combustion heat exchange units are connected through the connecting box body, the combustion heat exchange units are distributed around the connecting box body in a central symmetry manner, the outer parts of the connecting box body and the combustion heat exchange units are wrapped by the shell 5, heat insulation materials 3 are filled between the shell 5 and the connecting box body as well as between the shell and the combustion heat exchange units, heat dissipation is prevented, and the premixer is arranged at the upper part of the connecting box body;
the combustion heat exchange unit comprises an anti-backfire structure, a combustion chamber 40, a tail heat exchanger and an air inlet chamber 2, wherein two premixed gas inlet pipes 1 are welded on the side wall surface of the air inlet chamber 2; the anti-backfire structure is composed of an anti-backfire water chamber 35 and an anti-backfire air inlet channel 4, the anti-backfire air inlet channel 4 is embedded in the anti-backfire water chamber 35 through welding, the front end of the anti-backfire water chamber 35 is connected with the air inlet chamber 2, the rear end of the anti-backfire water chamber is connected with the combustion chamber 40, a tail heat exchanger is arranged at the outlet of the combustion chamber 40, the combustion chamber 40 and the tail heat exchanger are both arranged in the combustion chamber inner shell 31, and the air inlet chamber 2 is communicated with the combustion chamber 40 through the anti-backfire air inlet channel 4; the anti-backfire air inlet channel 4 is filled with small-pore porous medium materials 36; a plurality of heat exchange water chambers 39 are distributed in the inner shell of the combustion chamber 40 at intervals, the combustion chamber 40 is divided into a plurality of small combustion areas by the plurality of heat exchange water chambers 39, the small combustion areas are filled with non-uniform porous medium materials 34, and refractory bricks 9 are arranged at the upper end and the lower end of each small combustion area and close to the inner shell of the combustion chamber; the number of rows of the anti-backfire air inlet channels is the same as the number of small areas of the combustion chamber; a gap is reserved at the upstream of the combustion chamber and the part connected with the anti-backfire water chamber, an igniter electrode 32 is fixedly arranged in the gap, and simultaneously, premixed gas entering a small area of the combustion chamber can be ensured to be ignited;
the anti-backfire water chamber 35 is welded with an anti-backfire water chamber water inlet pipe 6 and an anti-backfire water chamber water outlet pipe 33, the heat exchange water chamber is welded with a heat exchange water chamber water outlet pipe 8 and a heat exchange water chamber water inlet pipe 21, two ends of the heat exchange water chamber water inlet pipe 21 are closed, an inlet and a plurality of outlets are arranged, the number of the outlets is consistent with that of the heat exchange water chamber 39, and each outlet is respectively communicated with one heat exchange water chamber; the water outlet pipe 33 of the anti-backfire water chamber is connected with the inlet of the water inlet pipe 21 of the heat exchange water chamber, and the outlets of a plurality of heat exchange water chambers of each combustion heat exchange unit are communicated with the water outlet pipe 8 of the heat exchange water chamber;
the tail heat exchanger comprises a tail heat exchange tube 29, a tail heat exchanger inlet header 24 and a tail heat exchanger outlet header 10, two ends of the tail heat exchange tube 29 are respectively welded on the tail heat exchanger inlet header 24 and the tail heat exchanger outlet header 10, and the tail heat exchange tube 29 is fixedly connected with the side wall of the combustion chamber inner shell; the outlet header 10 of the tail heat exchanger is connected with the water inlet pipe 6 of the anti-backfire water chamber through a connecting water pipe 7;
the connecting box body comprises a plurality of connecting box body side plates 15, a connecting box body top plate 16 and a connecting box body bottom plate 28, the number of the connecting box body side plates 15 is consistent with that of the combustion heat exchange units, box body spaces surrounded by the connecting box body side plates 15, the connecting box body top plate 16 and the connecting box body bottom plate 28 form a smoke collecting chamber, each connecting box body side plate 15 is welded with a side plate of a combustion chamber inner shell 31 of the corresponding combustion heat exchange unit, and the connecting box body top plate 16 and the connecting box body bottom plate 28 are welded with a top plate and a bottom plate of the combustion chamber inner shell of the corresponding combustion heat exchange unit; the bottom of the connecting box body is of a reverse pyramid structure, a cylindrical condensate water collecting chamber 27 is welded in the center of a bottom plate 28 of the connecting box body, and a drain pipe 25 and a smoke exhaust pipe 26 are welded on the condensate water collecting chamber;
an annular boiler inlet collecting pipe 22 is arranged at the bottom of the connecting box body, a boiler water inlet pipe 37 is welded on the boiler inlet collecting pipe, a plurality of water outlets which are consistent with the number of the combustion heat exchange units are uniformly distributed on the boiler inlet collecting pipe, the water outlets are connected with a tail heat exchanger inlet collecting pipe 24 of the corresponding combustion heat exchange unit, a plurality of water valves 23 which are consistent with the number of the combustion heat exchange units are arranged on the annular boiler inlet collecting pipe 22, and the normal operation of partial combustion heat exchange units can be realized according to the load requirement of the boiler; the top of the connecting box body is provided with an annular boiler outlet collecting pipe 11, a plurality of water inlets and a water outlet which are consistent with the quantity of the combustion heat exchange units are distributed on the boiler outlet collecting pipe 11, the water inlets are respectively connected with the water outlet pipes 8 of the heat exchange water chambers of the corresponding combustion heat exchange units, and the water outlet of the boiler outlet collecting pipe is welded with a hot water outlet pipe 38.
In the gas boiler based on the porous medium combustion technology, the premixer is used for mixing gas and air, and comprises a gas nozzle 20, an ejector 13, an air nozzle 19, a premixing chamber 14 and a premixed gas outlet pipe 17; the lower part of the premixing chamber 14 is fixedly connected with the upper surface of the connecting box body, two ejectors 13 are arranged on the side face, close to the top, of the premixing chamber 14, the included angle between the two ejectors 13 is 120 degrees, a plurality of premixed gas outlet pipes 17 are uniformly arranged on the side face, close to the bottom, of the premixing chamber 14, the number of the premixed gas outlet pipes 17 is twice that of combustion heat exchange units, the premixed gas outlet pipes 17 are connected with a premixed gas inlet pipe 1 of the gas inlet chamber through premixed gas connecting pipes 12, and each premixed gas connecting pipe 12 is provided with a stop valve 18, so that the working load of the gas boiler can be adjusted conveniently.
The number of the combustion heat exchange units is 2-12.
The heat exchange water chambers (see fig. 4) are in a cuboid structure, the number of the heat exchange water chambers in each combustion heat exchange unit is 4-20, and the water inlet pipe 21 of each heat exchange water chamber is a steel pipe with two closed ends and 1 inlet and 4-20 outlets.
The cross section width of each small combustion area in the combustion chamber is 10-30mm, and the depth is 60-500 mm.
The diameter of the anti-backfire air inlet channel is 10-25 mm.
The diameter of the tail heat exchange tube is 8-20 mm.
The cross sections of the air inlet chamber and the anti-backfire water chamber are square or rectangular, and (3-19) × (3-45) anti-backfire air inlet channels 4 are embedded in the anti-backfire water chamber 35 (see fig. 3), namely 3-19 rows and 3-45 lines are arranged, the row spacing is 20-70mm, the line spacing is 30-60mm, and the diameter is 10-25 mm.
The small-pore porous medium material has the pore density of 40PPI-60PPI and the porosity of 80-90%.
The pore density of the non-uniform porous medium material is 10PPI-40PPI, the pore density is non-uniformly distributed in the airflow direction in a small area of each combustion chamber, and the non-uniform porous medium material is formed by sequentially overlapping 3-20 rectangular sheet-shaped porous media with the thickness of 10-40 mm.
And the size of a gap left at the part of the upstream of the combustion chamber, which is connected with the tempering-proof water chamber, is 4-8 mm.
The invention relates to a flow mode of water in a gas boiler based on a porous medium combustion technology, which comprises the following steps: boiler water inlet pipe 37 → boiler inlet header 22 → tail heat exchanger inlet header 24 → tail heat exchange pipe 29 → tail heat exchanger outlet header 10 → connecting water pipe 7 → anti-flashback water chamber water inlet pipe 6 → anti-flashback water chamber 35 → anti-flashback water chamber water outlet pipe 33 → heat exchange water chamber water inlet pipe 21 → heat exchange water chamber 39 → heat exchange water chamber water outlet pipe 8 → boiler outlet header 10 → hot water outlet pipe 38.
The tail heat exchange tube 29 in the invention is composed of 10-80 layers of snake-shaped heat exchange tubes, the number of layers of the tail heat exchange tubes is related to the size of the combustion chamber, and specifically, the larger the power of the gas furnace is, the larger the height of the combustion chamber is, and the more the tail heat exchange tubes can be accommodated. The number of the heat exchange water chambers in the combustion chamber is 4-20, the specific number requirement is related to the power of a single combustion heat exchange unit, each combustion heat exchange unit is transversely divided into a plurality of small combustion areas by a plurality of heat exchange water chambers, the width of the cross section of each small combustion area is required and is generally 10-30mm, the width of each heat exchange water chamber is 10-40mm, the combustion chamber required is large when the power of the combustion heat exchange unit is high, the number of the small combustion areas divided by the heat exchange water chambers is large, and 3-19 small combustion areas can be provided. The number of the opened valves of the water valve 23 is consistent with the number of the started combustion heat exchange units, so that cold water is prevented from entering the combustion heat exchange units which do not work, and normal operation of part of the combustion heat exchange units can be realized according to the load requirement of the boiler.
The heterogeneous porous dielectric material 34 and the small-pore porous dielectric material 36 can be alumina, silicon carbide or zirconia, and the like, and can resist high temperature of more than 1000 ℃.
Example 1
The structure and shape of the gas boiler based on the porous medium combustion technology of the embodiment are shown in figures 1-4.
The gas boiler based on the porous medium combustion technology comprises a premixer, a plurality of combustion heat exchange units and a connecting box body; the combustion heat exchange units are connected through the connecting box body, the combustion heat exchange units are distributed around the connecting box body in a central symmetry manner, the outer parts of the connecting box body and the combustion heat exchange units are wrapped by the shell 5, heat insulation materials 3 are filled between the shell 5 and the connecting box body as well as between the shell and the combustion heat exchange units, heat dissipation is prevented, and the premixer is arranged at the upper part of the connecting box body;
the combustion heat exchange unit comprises an anti-backfire structure, a combustion chamber 40, a tail heat exchanger and an air inlet chamber 2, wherein two premixed gas inlet pipes 1 are welded on the side wall surface of the air inlet chamber 2; the anti-backfire structure is composed of an anti-backfire water chamber 35 and an anti-backfire air inlet channel 4, the anti-backfire air inlet channel 4 is embedded in the anti-backfire water chamber 35 through welding, the front end of the anti-backfire water chamber 35 is connected with the air inlet chamber 2, the rear end of the anti-backfire water chamber is connected with the combustion chamber 40, a tail heat exchanger is arranged at the outlet of the combustion chamber 40, the combustion chamber 40 and the tail heat exchanger are both arranged in the combustion chamber inner shell 31, and the air inlet chamber 2 is communicated with the combustion chamber 40 through the anti-backfire air inlet channel 4; the anti-backfire air inlet channel 4 is filled with small-pore porous medium materials 36; a plurality of heat exchange water chambers 39 are distributed in the inner shell of the combustion chamber 40 at intervals, the combustion chamber 40 is divided into a plurality of small combustion areas by the plurality of heat exchange water chambers 39, the small combustion areas are filled with non-uniform porous medium materials 34, and refractory bricks 9 are arranged at the upper end and the lower end of each small combustion area and close to the inner shell of the combustion chamber; the number of rows of the anti-backfire air inlet channels is the same as the number of small areas of the combustion chamber; a gap is reserved at the upstream of the combustion chamber and the part connected with the anti-backfire water chamber, an igniter electrode 32 is fixedly arranged in the gap, and simultaneously, premixed gas entering a small area of the combustion chamber can be ensured to be ignited;
the anti-backfire water chamber 35 is welded with an anti-backfire water chamber water inlet pipe 6 and an anti-backfire water chamber water outlet pipe 33, the heat exchange water chamber is welded with a heat exchange water chamber water outlet pipe 8 and a heat exchange water chamber water inlet pipe 21, two ends of the heat exchange water chamber water inlet pipe 21 are closed, an inlet and a plurality of outlets are arranged, the number of the outlets is consistent with that of the heat exchange water chamber 39, and each outlet is respectively communicated with one heat exchange water chamber; the water outlet pipe 33 of the anti-backfire water chamber is connected with the inlet of the water inlet pipe 21 of the heat exchange water chamber, and the outlets of a plurality of heat exchange water chambers of each combustion heat exchange unit are communicated with the water outlet pipe 8 of the heat exchange water chamber;
the tail heat exchanger comprises a tail heat exchange tube 29, a tail heat exchanger inlet header 24 and a tail heat exchanger outlet header 10, two ends of the tail heat exchange tube 29 are respectively welded on the tail heat exchanger inlet header 24 and the tail heat exchanger outlet header 10, and the tail heat exchange tube 29 is fixedly connected with the side wall of the combustion chamber inner shell; the outlet header 10 of the tail heat exchanger is connected with the water inlet pipe 6 of the anti-backfire water chamber through a connecting water pipe 7;
the connecting box body comprises a plurality of connecting box body side plates 15, a connecting box body top plate 16 and a connecting box body bottom plate 28, the number of the connecting box body side plates 15 is consistent with that of the combustion heat exchange units, box body spaces surrounded by the connecting box body side plates 15, the connecting box body top plate 16 and the connecting box body bottom plate 28 form a smoke collecting chamber, each connecting box body side plate 15 is welded with a side plate of a combustion chamber inner shell 31 of the corresponding combustion heat exchange unit, and the connecting box body top plate 16 and the connecting box body bottom plate 28 are welded with a top plate and a bottom plate of the combustion chamber inner shell of the corresponding combustion heat exchange unit; the bottom of the connecting box body is of a reverse pyramid structure, a cylindrical condensate water collecting chamber 27 is welded in the center of a bottom plate 28 of the connecting box body, and a drain pipe 25 and a smoke exhaust pipe 26 are welded on the condensate water collecting chamber;
an annular boiler inlet collecting pipe 22 is arranged at the bottom of the connecting box body, a boiler water inlet pipe 37 is welded on the boiler inlet collecting pipe, a plurality of water outlets which are consistent with the number of the combustion heat exchange units are uniformly distributed on the boiler inlet collecting pipe, the water outlets are connected with a tail heat exchanger inlet collecting pipe 24 of the corresponding combustion heat exchange unit, a plurality of water valves 23 which are consistent with the number of the combustion heat exchange units are arranged on the annular boiler inlet collecting pipe 22, and the normal operation of partial combustion heat exchange units can be realized according to the load requirement of the boiler; the top of the connecting box body is provided with an annular boiler outlet collecting pipe 11, a plurality of water inlets and a water outlet which are consistent with the quantity of the combustion heat exchange units are distributed on the boiler outlet collecting pipe 11, the water inlets are respectively connected with the water outlet pipes 8 of the heat exchange water chambers of the corresponding combustion heat exchange units, and the water outlet of the boiler outlet collecting pipe is welded with a hot water outlet pipe 38.
The gas boiler based on porous medium combustion technology of this embodiment has 4 burning heat transfer units, and every burning heat transfer unit has 4 heat transfer hydroecium 39, encloses into 3 burning small region, and it has 3 rows of anti-backfire inlet channel 4 to correspond. The size of the heat exchange water chamber 39 is 235 × 90 × 30mm, the height of the enclosed small combustion area is 235mm, the depth is 90mm, and the width is 30 mm. The diameter of the anti-backfire air inlet channel 4 is 16mm, the row spacing is 60mm, and the line spacing is 47 mm. The non-uniform porous dielectric material 34 and the small pore porous dielectric material 36 are both alumina. The water inlet pipe 21 of the heat exchange water chamber is a steel pipe with two closed ends and 4 outlets, and the outlet ends are respectively communicated with the 4 heat exchange water chambers 39. The combustion chamber inner shell 31 is formed by welding 4 stainless steel plates (1 top plate, 1 bottom plate and 2 side plates), and the size of a gap left at the part, connected with the tempering water proof chamber, of the upstream of the combustion chamber is 8 mm.
In the embodiment, the tail heat exchange tube 29 is composed of 12 layers of snakelike heat exchange tubes, two ends of each layer of heat exchange tube are respectively welded on the inlet collecting tube 24 and the outlet collecting tube 10 of the tail heat exchanger, and the tail heat exchange tube 29 is fixed on the combustion chamber inner shell 31 through the positioning piece 30 in a spot welding mode.
In the embodiment, the connecting box body is formed by welding 4 side plates 15, 1 top plate 16 and 1 bottom plate 28 to form a box body structure, so that a smoke collecting chamber is formed; the side plates of the connecting box body 15 and the side plates of the combustion chamber inner shell 31 of every two combustion heat exchange units are welded together, and the outer shell 5 is divided into a side plate, a top plate and a bottom plate which are fixedly connected by screws respectively. 4 water outlets are uniformly distributed on the boiler inlet header 22, 4 water valves 23 are installed, and normal operation of the partial combustion heat exchange unit can be realized according to the load requirement of the boiler. And 4 water inlets and one water outlet are arranged on the boiler outlet header 11, and the 4 water inlets are respectively connected with the water outlet pipes 8 of the heat exchange water chambers of the 4 combustion heat exchange units.
The rated power of the gas-fired boiler based on the porous medium combustion technology is 160kW, and the thermal efficiency of the boiler can reach 96% -107%.
Example 2
The structure of each part of the gas boiler based on the porous medium combustion technology in the embodiment is connected with that in the embodiment 1, the difference is that the premixer comprises a gas nozzle 20, an ejector 13, an air nozzle 19, a premixing chamber 14 and a premixed gas outlet pipe 17; the lower part of the premixing chamber 14 is fixedly connected with the upper surface of the connecting box body, two ejectors 13 are arranged on the side surface, close to the top, of the premixing chamber 14, the included angle between the two ejectors 13 is 120 degrees, 8 premixed gas outlet pipes 17 are uniformly arranged on the side surface, close to the bottom, of the premixing chamber 14, the premixed gas outlet pipes 17 are connected with a premixed gas inlet pipe 1 of the gas inlet chamber through premixed gas connecting pipes 12, each premixed gas connecting pipe 12 is provided with a stop valve 18, and the work load of the gas boiler based on the porous medium combustion technology can be adjusted conveniently.
Example 3
The present embodiment is a gas boiler based on porous medium combustion technology, and the structural connection of each part is the same as that in embodiment 1, except that the gas boiler based on porous medium combustion technology in this embodiment has 6 combustion heat exchange units, fig. 5 is a schematic top-view cross-sectional view of a connection box body thereof, the cross-section in the figure is a side plate 15 of the connection box body, and there are 6 side plates in total, and each side plate 15 is connected with every two combustion heat exchange units.
In the gas boiler based on the porous medium combustion technology, related raw materials, parts and installation methods thereof are all well known in the technical field.
Nothing in this specification is said to apply to the prior art.

Claims (10)

1.一种基于多孔介质燃烧技术的燃气锅炉,包括预混器、若干数量的燃烧换热单元和连接箱体;所述若干数量的燃烧换热单元通过连接箱体连接,燃烧换热单元围绕连接箱体呈中心对称分布,连接箱体和燃烧换热单元外部包裹有外壳,在外壳与连接箱体和燃烧换热单元之间填充有保温材料,预混器设置在连接箱体的上部;1. A gas boiler based on porous medium combustion technology, comprising a premixer, a number of combustion heat exchange units and a connection box; the number of combustion heat exchange units are connected through the connection box, and the combustion heat exchange unit surrounds the The connection box is symmetrically distributed in the center, the outer shell of the connection box and the combustion heat exchange unit is wrapped, and the insulation material is filled between the outer shell, the connection box and the combustion heat exchange unit, and the premixer is arranged on the upper part of the connection box; 所述燃烧换热单元包括防回火结构、燃烧室、尾部换热器和进气室,所述进气室的侧壁面焊接有两个预混气体进口管;所述防回火结构由防回火水室和防回火进气通道构成,防回火进气通道通过焊接嵌入在防回火水室中,防回火水室前端与进气室连接,在防回火水室后端连接燃烧室,在燃烧室的出口布置有尾部换热器,燃烧室和尾部换热器均置于燃烧室内壳中,通过防回火进气通道联通进气室和燃烧室;在防回火进气通道内填满小孔隙多孔介质材料;所述燃烧室的内壳内间隔分布有若干数量的换热水室,燃烧室由若干数量的换热水室分割成多个燃烧小区域,在每个燃烧室小区域内填充有非均匀多孔介质材料,在每个燃烧室小区域的上下两端,且靠近燃烧室内壳处设置耐火砖;防回火进气通道的列数与燃烧室小区域的数量相同;在燃烧室上游,且与防回火水室相连的部分留有空隙,在此空隙内固定安装点火器电极;The combustion heat exchange unit includes an anti-tempering structure, a combustion chamber, a rear heat exchanger and an intake chamber, and two premixed gas inlet pipes are welded on the side wall surface of the intake chamber; The tempering water chamber and the anti-tempering air intake channel are formed. The anti-tempering air intake channel is embedded in the anti-tempering water chamber by welding. The combustion chamber is connected, and a rear heat exchanger is arranged at the outlet of the combustion chamber. Both the combustion chamber and the rear heat exchanger are placed in the combustion inner shell, and the intake chamber and the combustion chamber are communicated through the anti-backfire intake passage; The intake passage is filled with porous medium material with small pores; a number of hot water exchange chambers are distributed at intervals in the inner shell of the combustion chamber, and the combustion chamber is divided into a plurality of small combustion areas by a number of hot water exchange chambers. Each small area of the combustion chamber is filled with non-uniform porous media material, and refractory bricks are arranged at the upper and lower ends of each small area of the combustion chamber, and near the inner casing of the combustion chamber; The number is the same; there is a gap in the upstream of the combustion chamber and the part connected to the anti-backfire water chamber, and the igniter electrode is fixedly installed in this gap; 防回火水室上焊接有防回火水室进水管和防回火水室出水管,换热水室上焊接有换热水室出水管和换热水室进水管,所述换热水室进水管的两端封闭,并设有一个入口和若干数量个出口,出口的数量与换热水室的数量一致,每个出口分别联通一个换热水室;防回火水室出水管与换热水室进水管的入口连接,每个燃烧换热单元的若干数量的换热水室的出口均与换热水室出水管相联通;The anti-tempering water chamber is welded with an anti-tempering water chamber inlet pipe and an anti-tempering water chamber outlet pipe, and a hot water exchange chamber outlet pipe and a hot water exchange chamber inlet pipe are welded on the hot water exchange chamber. The two ends of the water inlet pipe of the chamber are closed, and there is an inlet and a number of outlets. The number of outlets is consistent with the number of hot water exchange chambers, and each outlet is connected to a hot water exchange chamber; The inlets of the water inlet pipes of the hot water exchange chambers are connected, and the outlets of a certain number of the hot water exchange chambers of each combustion heat exchange unit are connected with the water outlet pipes of the hot water exchange chambers; 所述尾部换热器包括尾部换热管、尾部换热器入口集管和尾部换热器出口集管,尾部换热管的两端分别焊接在尾部换热器入口集管和尾部换热器出口集管上,尾部换热管与燃烧室内壳的侧壁固定连接;尾部换热器出口集管和防回火水室进水管之间通过连接水管相连;The rear heat exchanger includes a rear heat exchange tube, an inlet header of the rear heat exchanger and an outlet header of the rear heat exchanger, and both ends of the rear heat exchange tube are welded to the inlet header of the rear heat exchanger and the rear heat exchanger respectively. On the outlet header, the rear heat exchange tube is fixedly connected with the side wall of the combustion inner shell; the outlet header of the rear heat exchanger and the water inlet pipe of the anti-backfire water chamber are connected by a connecting water pipe; 所述连接箱体包括若干数量的连接箱体侧板、连接箱体顶板和连接箱体底板,所述连接箱体侧板的数量与燃烧换热单元的数量一致,若干数量的连接箱体侧板、连接箱体顶板和连接箱体底板所围成的箱体空间构成烟气汇集室,每个连接箱体侧板分别与相应的燃烧换热单元的燃烧室内壳的侧板焊接在一起,连接箱体顶板和连接箱体底板分别与相应的燃烧换热单元的燃烧室内壳的顶板和底板焊接在一起;连接箱体的底部为倒棱锥状结构,连接箱体底板中心焊接有圆筒状的冷凝水汇集室,冷凝水汇集室上焊接有排水管和排烟管;The connection box includes a number of side plates of the connection box, the top plate of the connection box and the bottom plate of the connection box. The number of the side plates of the connection box is consistent with the number of the combustion heat exchange units. The box space enclosed by the plate, the top plate of the connecting box and the bottom plate of the connecting box constitutes a flue gas collection chamber, and each side plate of the connecting box is respectively welded with the side plate of the combustion inner shell of the corresponding combustion heat exchange unit. The top plate of the connecting box body and the bottom plate of the connecting box body are respectively welded with the top plate and the bottom plate of the combustion inner shell of the corresponding combustion heat exchange unit; The condensed water collection chamber is welded with a drain pipe and a smoke exhaust pipe; 连接箱体底部设置环状的锅炉入口集管,锅炉入口集管上焊接有锅炉进水管,锅炉入口集管上设置有与燃烧换热单元数量一致的若干数量的出水口,该出水口与相应的燃烧换热单元的尾部换热器入口集管连接,环状的锅炉入口集管上安装与燃烧换热单元数量一致的若干数量的水阀;连接箱体的顶部设置有环状的锅炉出口集管,锅炉出口集管上设置有与燃烧换热单元数量一致的若干个进水口和一个出水口,该进水口分别与相应燃烧换热单元的换热水室出水管连接,锅炉出水集管的出水口上焊接有热水出水管。A ring-shaped boiler inlet header is arranged at the bottom of the connection box. The boiler inlet header is welded with a boiler water inlet pipe. The boiler inlet header is provided with a number of water outlets consistent with the number of combustion heat exchange units. The inlet header of the rear heat exchanger of the combustion heat exchange unit is connected, and the annular boiler inlet header is installed with a number of water valves that are consistent with the number of combustion heat exchange units; the top of the connection box is provided with an annular boiler outlet Header, the boiler outlet header is provided with a number of water inlets and a water outlet consistent with the number of combustion heat exchange units, the water inlets are respectively connected with the water outlet pipes of the hot water exchange chamber of the corresponding combustion heat exchange units, and the boiler outlet header pipes A hot water outlet pipe is welded on the water outlet. 2.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述预混器包括燃气喷嘴、引射器、空气喷嘴、预混室和预混气体出口管;在预混室的下部与连接箱体的上表面固定连接,在预混室靠近顶部的侧面上设置有两个引射器,两个引射器之间的夹角为120°,在预混室靠近底部的侧面上均匀布置有若干数量的预混气体出口管,预混气体出口管的数量为燃烧换热单元数量的两倍,预混气体出口管通过预混气体联络管与进气室的预混气体进口管连接,每个预混气体联络管上均安装有截止阀。2. The gas boiler based on porous media combustion technology according to claim 1, characterized in that the premixer comprises a gas nozzle, an ejector, an air nozzle, a premix chamber and a premix gas outlet pipe; The lower part of the chamber is fixedly connected with the upper surface of the connection box, two ejectors are arranged on the side of the premixing chamber near the top, and the included angle between the two ejectors is 120°, and the premixing chamber is close to the bottom There are a number of premixed gas outlet pipes evenly arranged on the side of the unit. The number of premixed gas outlet pipes is twice the number of combustion heat exchange units. The gas inlet pipe is connected, and a stop valve is installed on each premixed gas connection pipe. 3.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述燃烧换热单元的数量为2-12个。3 . The gas boiler based on porous media combustion technology according to claim 1 , wherein the number of the combustion heat exchange units is 2-12. 4 . 4.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述换热水室的形状为长方体结构,在每个燃烧换热单元中换热水室的个数为4-20个。4. The gas boiler based on porous medium combustion technology according to claim 1, wherein the shape of the water exchange chamber is a rectangular parallelepiped structure, and the number of the water exchange chambers in each combustion heat exchange unit is 4 -20. 5.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述燃烧室内每个燃烧小区域的横截面宽度为10-30mm,深度为60-500mm。5 . The gas boiler based on porous media combustion technology according to claim 1 , wherein the cross-sectional width of each small combustion area in the combustion chamber is 10-30 mm, and the depth is 60-500 mm. 6 . 6.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于防回火进气通道的直径为10-25mm。6. The gas boiler based on porous media combustion technology according to claim 1, characterized in that the diameter of the anti-tempering inlet passage is 10-25 mm. 7.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述尾部换热管直径为8-20mm。7. The gas-fired boiler based on porous media combustion technology according to claim 1, characterized in that the diameter of the tail heat exchange tube is 8-20 mm. 8.根据权利要求1所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述进气室和防回火水室的截面为正方形或长方形。8 . The gas boiler based on porous media combustion technology according to claim 1 , wherein the cross-sections of the intake chamber and the anti-backfire water chamber are square or rectangular. 9 . 9.根据权利要求1-8任一所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述小孔隙多孔介质材料的孔隙密度为40PPI-60PPI,孔隙率为80%-90%。9 . The gas boiler based on porous media combustion technology according to claim 1 , wherein the porous media material with small pores has a pore density of 40PPI-60PPI, and a porosity of 80%-90%. 10 . 10.根据权利要求1-8任一所述的基于多孔介质燃烧技术的燃气锅炉,其特征在于所述非均匀多孔介质材料的孔隙密度为10PPI-40PPI,在每个燃烧室小区域内,在气流方向上孔隙密度呈非均匀分布,由3-20块厚度为10-40mm的长方形片状多孔介质依次叠加而成。10. The gas boiler based on porous media combustion technology according to any one of claims 1-8, wherein the pore density of the non-uniform porous media material is 10PPI-40PPI, and in a small area of each combustion chamber, in the airflow The pore density is unevenly distributed in the direction, and it is formed by stacking 3-20 rectangular sheet-like porous media with a thickness of 10-40mm in turn.
CN201610807386.6A 2016-09-07 2016-09-07 Gas boiler based on porous media combustion technology Active CN106288370B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610807386.6A CN106288370B (en) 2016-09-07 2016-09-07 Gas boiler based on porous media combustion technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610807386.6A CN106288370B (en) 2016-09-07 2016-09-07 Gas boiler based on porous media combustion technology

Publications (2)

Publication Number Publication Date
CN106288370A CN106288370A (en) 2017-01-04
CN106288370B true CN106288370B (en) 2021-09-24

Family

ID=57710968

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610807386.6A Active CN106288370B (en) 2016-09-07 2016-09-07 Gas boiler based on porous media combustion technology

Country Status (1)

Country Link
CN (1) CN106288370B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110360568A (en) * 2019-08-23 2019-10-22 北京泷涛环境科技有限公司 A kind of low nitrogen combustion apparatus and method
CN114017762A (en) * 2021-11-09 2022-02-08 江苏双良锅炉有限公司 Horizontal internal combustion steam boiler with porous ceramic medium combustion

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2100580U (en) * 1990-02-22 1992-04-01 孙荣清 Double-functional living boiler
CN2335095Y (en) * 1998-07-17 1999-08-25 戴华斌 Building-block type honeycomb briquet atmospheric pressure water-heating boiler
CN2484481Y (en) * 2001-06-06 2002-04-03 浙江大学 Gradual-change porous-medium burner
CN2534519Y (en) * 2002-04-01 2003-02-05 凤城市百利锅炉制造有限公司 Atmospheric pressure water heating coal boiler
CN2713375Y (en) * 2003-10-16 2005-07-27 广州迪森热能设备有限公司 A hot water boiler
CN101566386A (en) * 2009-03-18 2009-10-28 河北工业大学 Porous-medium gas hot water heater
CN102748860A (en) * 2012-07-17 2012-10-24 苏州威博特能源环保科技有限公司 Combined high-power condensing boiler and control method thereof
CN103090539A (en) * 2011-11-08 2013-05-08 上海康洪精密机械有限公司 Double-output composite boiler
CN204438099U (en) * 2014-10-22 2015-07-01 北京神雾环境能源科技集团股份有限公司 Heat storage type porous medium burner assembly
CN204534588U (en) * 2015-04-20 2015-08-05 河北工业大学 A kind of water-cooled gas burner
CN205424884U (en) * 2016-04-01 2016-08-03 温州博远工业设计有限公司 Residual heat from flue gas of firepower factory device
CN206001681U (en) * 2016-09-07 2017-03-08 河北工业大学 A kind of porous-medium gas hot boiler

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR940008394B1 (en) * 1991-12-21 1994-09-14 주식회사 금성사 Gas Boiler with Porous-medium
DE4322109C2 (en) * 1993-07-02 2001-02-22 Franz Durst Burner for a gas / air mixture
CN2261004Y (en) * 1996-04-30 1997-08-27 双鸭山东方工业公司 High-efficiency after-heat exchanger
CN100472131C (en) * 2003-07-30 2009-03-25 巴布考克日立株式会社 Heat exchanger tube panel module, and method of constructing exhaust heat recovery boiler using the module
CN101655279A (en) * 2009-05-29 2010-02-24 李金才 Multi-stage rotating energy-saving dust and harmful substance removing vertical boiler
CN101968220B (en) * 2010-10-28 2012-01-11 河北工业大学 Low nitrogen oxide burning process as well as burning device and application
CN102168888B (en) * 2011-02-25 2013-02-27 清华大学 A contact type low temperature flue gas waste heat deep recovery and utilization system
US8818252B2 (en) * 2012-10-29 2014-08-26 Eastman Kodak Company Toner fixer transporting medium through heating liquid
CN103062770A (en) * 2013-01-16 2013-04-24 浙江大学 High-temperature gas generating device on basis of porous medium combustion and heat storage
CN203068491U (en) * 2013-01-17 2013-07-17 杨群峰 Vertical type water-fire pressure-bearing boiler
CN103277781B (en) * 2013-04-16 2014-12-10 西安交通大学 Embedded modularized assembly water pipe fuel oil and fuel gas boiler
CN203478592U (en) * 2013-10-11 2014-03-12 河北群翔采暖设备有限公司 Atmosphere-type fuel gas module energy-saving environment-protecting boiler
DE102014205208B4 (en) * 2014-03-20 2024-09-26 Eberspächer Climate Control Systems GmbH Vehicle heater

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2100580U (en) * 1990-02-22 1992-04-01 孙荣清 Double-functional living boiler
CN2335095Y (en) * 1998-07-17 1999-08-25 戴华斌 Building-block type honeycomb briquet atmospheric pressure water-heating boiler
CN2484481Y (en) * 2001-06-06 2002-04-03 浙江大学 Gradual-change porous-medium burner
CN2534519Y (en) * 2002-04-01 2003-02-05 凤城市百利锅炉制造有限公司 Atmospheric pressure water heating coal boiler
CN2713375Y (en) * 2003-10-16 2005-07-27 广州迪森热能设备有限公司 A hot water boiler
CN101566386A (en) * 2009-03-18 2009-10-28 河北工业大学 Porous-medium gas hot water heater
CN103090539A (en) * 2011-11-08 2013-05-08 上海康洪精密机械有限公司 Double-output composite boiler
CN102748860A (en) * 2012-07-17 2012-10-24 苏州威博特能源环保科技有限公司 Combined high-power condensing boiler and control method thereof
CN204438099U (en) * 2014-10-22 2015-07-01 北京神雾环境能源科技集团股份有限公司 Heat storage type porous medium burner assembly
CN204534588U (en) * 2015-04-20 2015-08-05 河北工业大学 A kind of water-cooled gas burner
CN205424884U (en) * 2016-04-01 2016-08-03 温州博远工业设计有限公司 Residual heat from flue gas of firepower factory device
CN206001681U (en) * 2016-09-07 2017-03-08 河北工业大学 A kind of porous-medium gas hot boiler

Also Published As

Publication number Publication date
CN106288370A (en) 2017-01-04

Similar Documents

Publication Publication Date Title
CN104764017B (en) A kind of water-cooled gas burner
WO2016107383A1 (en) Porous medium burner with stacked bed structure
CN211261292U (en) Novel full premix heat exchanger
CN202747616U (en) Plate type gas combustion and condensation type hot water boiler
CN204534588U (en) A kind of water-cooled gas burner
CN101566386B (en) Porous-medium gas hot water heater
CN106288370B (en) Gas boiler based on porous media combustion technology
CN110822714B (en) A gas condensing boiler with narrow gap combustion and heat exchange
CN111102569A (en) Porous medium burning low-nitrogen gas boiler system and heat exchange system
CN206001681U (en) A kind of porous-medium gas hot boiler
CN102168886A (en) Combustion furnace for flue-cured bulk curing barn
CN202452466U (en) Vertical type steam boiler
CN201072221Y (en) Smoke canal pre-heating type gas water heater
CN113375141A (en) Energy-efficient steam boiler
CN209196896U (en) Combustion heat exchanger
CN211450920U (en) Porous medium burning low-nitrogen gas boiler system and heat exchange system
CN201945017U (en) High-efficiency and energy-saving water heating boiler
CN208205406U (en) A kind of burning energy-saving boiler
CN106052112A (en) Vertical type three-pass fuel gas normal-pressure hot-water boiler body
CN207849339U (en) A kind of three backhaul list ontology heat exchange structures of steam boiler
CN205939674U (en) Extreme misery pipe boiler
CN105371488A (en) Tubular hot air heat exchange device
CN205332515U (en) Hot -blast heat transfer device of shell and tube
CN103175231A (en) Heat integration gas furnace device
CN203375682U (en) Vertical type coal-fired hot-water boiler

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20211213

Address after: 075000 zone 505 / A, floor 5, block B, business incubation building, No. 8, Shenkong Road, high tech Industrial Development Zone, Zhangjiakou City, Hebei Province

Patentee after: Hebei Hongyu Energy Technology Co.,Ltd.

Address before: 300130 No. 8, Hebei University of Technology, Tianjin, Hongqiao No. 330

Patentee before: Hebei University of Technology

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20220817

Address after: 076471 room 407, management committee building, Zhangbei Economic Development Zone, Zhangjiakou City, Hebei Province

Patentee after: Hebei Hongtan Energy Technology Co., Ltd.

Address before: 075000 zone 505 / A, floor 5, block B, business incubation building, No. 8, Shenkong Road, high tech Industrial Development Zone, Zhangjiakou City, Hebei Province

Patentee before: Hebei Hongyu Energy Technology Co.,Ltd.