CN101251300A - Pipe type heating furnace - Google Patents
Pipe type heating furnace Download PDFInfo
- Publication number
- CN101251300A CN101251300A CNA2008100197654A CN200810019765A CN101251300A CN 101251300 A CN101251300 A CN 101251300A CN A2008100197654 A CNA2008100197654 A CN A2008100197654A CN 200810019765 A CN200810019765 A CN 200810019765A CN 101251300 A CN101251300 A CN 101251300A
- Authority
- CN
- China
- Prior art keywords
- regenerator
- furnace
- heater
- burner
- tubular heater
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Air Supply (AREA)
Abstract
The invention relates to a tube type heating furnace, which comprises a radiation heating chamber and a burner, wherein, the radiation heating chamber mainly comprises a furnace body, a furnace chamber and a furnace pipe which is arranged in the furnace chamber. The invention is characterized in that two communicated regenerators are arranged on the outer side of the furnace body, comprise outerwalls and ceramic regenerative bodies, and are respectively connected with a two-position, four-way switch valve through an aeration pipe; the two-position, four-way switch valve is also connected with an air-input tube and a smoke-output tube. The burner is arranged in a communicating section where the regenerators are connected with the furnace body. The tube type heating furnace has the advantages of the ability to reduce the emissions of acid gases such as SO2,NOx, etc., small size, light weight, small floor area and low production cost.
Description
One, technical field
The present invention relates to the firing equipment that a kind of petrochemical industry and Coal Chemical Industry are produced, specifically a kind of tubular heater.
Two, background technology
Tubular heater in petrochemical industry and Coal Chemical Industry production industry mainly is made up of radiation heating chamber, burner, convection cell at present; The radiation heating chamber comprises body of heater, boiler tube, and convection cell comprises outer wall and convection tube, and radiation heating chamber and convection cell are communicated with; Convection cell is low to the utilization rate of fume afterheat in the present tubular heater, and the smog discharge temperature height for further utilizing fume afterheat, also will install tubular type combustion air preheater or steam generator additional and make exhaust gas temperature be reduced to below 150 ℃; Make tubular heater volume, weight and floor space all very big thus, the production cost height; And when exhaust gas temperature is reduced to below 150 ℃, SO in the flue gas
2, NO
xThe dew point lye that produces Deng sour gas can produce dew point corrosion to convection tube in the convection cell and chimney, thereby reduces the service life of tubular heater; When exhaust gas temperature is higher than 150 ℃, the SO in the flue gas
2, NO
xDeng sour gas cognition environment is polluted.
Three, technology contents
At above-mentioned shortcoming, the object of the present invention is to provide and a kind ofly can reduce SO in the flue gas
2, NO
xThe tubular heater that discharging, volume, weight and floor space are little and production cost is low Deng sour gas.
Technology contents of the present invention is: a kind of tubular heater, comprise radiation heating chamber and burner, the radiation heating chamber mainly is made of body of heater, furnace chamber and boiler tube, and boiler tube is installed in the furnace chamber, it is characterized in that in the body of heater outside connection two regenerator being installed, regenerator comprises outer wall and ceramic heat storage body; Two regenerator link to each other with 24 direction changeover valves by a breather pipe respectively, also are connected with air input pipe and flue gas efferent duct on 24 direction changeover valves; Burner is installed in regenerator and the Connectivity Section that body of heater links to each other.
For improving the heat transfer thermal efficiency of tubular heater, be provided with more than one partition wall in the furnace chamber between two regenerator, furnace chamber is partitioned into two Room or multicell, adjacent two Room communicate.
For preventing that the combustion flame that burner produces from producing damage to boiler tube, above Connectivity Section that regenerator links to each other with body of heater, a flame controller is installed; The flame controller can be a metal drum, has smoke hole (5.1) at the upper end of metal drum bucket wall, and the lower end is an open ports (5.2); For increasing the radiation heating effect of metal drum, the isometrical or aperture that has closeness increase up and down at the metal drum sidewall has little of big hole.
After exhaust gas temperature drops to below 150 ℃, can produce the dew point lye,, on regenerator, be connected and installed with a dew point liquid gathering-device for the dew point lye being drained.
The ceramic heat storage body that adopts among the present invention can be sphere or honeycombed.
For carrying out radiant heat transfer in the furnace chamber space that makes full use of radiation chamber, boiler tube can change coiled pipe into by original single arrangement along inboard wall of furnace body and arrange arrangement more.
The ceramic heat storage body withstand corrosion that adopts among the present invention and can fully hold the receipts fume afterheat drops to below 150 ℃ exhaust gas temperature, even can arrive normal temperature; SO in the flue gas
2, NO
xCollect by the dew point liquid gathering-device Deng the dew point lye that sour gas produces, reach the environmental-protection function of energy-saving and emission-reduction, can eliminate of the corrosion of warm dew point lye thus, also reduced SO equipment
2, NO
xDischarging, thereby lower atmosphere pollution.
Tubular heater of the present invention has saved convection cell, air preheater and heat retrieving apparatus, only keeps the radiation heating chamber, makes full use of high efficient radiation and conducts heat, and utilize two regenerator alternately to heat supply of radiation heating chamber and recovery fume afterheat; Air can reach 800 ℃ even higher by the regenerator temperature after heating, this high temperature air burns again and from the fuel mix of burner, its flame boundary is no longer obvious, make the pure radiant type that is heated to be in the radiation chamber, evenly heat intensity, fuel economy and furnace heat transfer efficient in furnace temperature uniformity, the stove have been improved, the raising of evenly heat intensity and furnace heat transfer efficient can reduce heat transfer area in furnace temperature uniformity, the stove, makes the volume-diminished of heating furnace, reduces floor space; Also make the flow process of the interior medium of boiler tube shorten, the use amount that can save boiler tube thus reduces construction cost.
Because the air themperature that thermal afterburning burns more than or equal to 800 ℃, is low excess air coefficient burning, its coefficient can reach 1.05, has played effect of saving energy thus, has also reduced SO simultaneously in the present invention
2, NO
xDeng the generation of sour gas, play the function of reduction of discharging.
The burner of and arranged on left and right sides takes turns to operate among the present invention, and flue gas reciprocating type flowing in furnace chamber carried out radiation heating to boiler tube, thereby makes temperature field in furnace even, improved fuel economy and furnace heat transfer efficient.
The advantage that the present invention is compared with prior art had is:
(1), the present invention saved convection cell, air preheater and heat retrieving apparatus, and radiation heating chamber and regenerator are only arranged, stove profile and structure are simpler, load on an equal basis stove volume, weight and floor space significantly reduce low cost of manufacture.
(2), the present invention finishes recovery to the high-temperature flue gas waste heat by regenerator, makes flue gas can reach the normal temperature discharging, and makes the SO that atmosphere is polluted in the flue gas
2, NO
xDeng sour gas, separate collection and treatment in the following condensation of dew point, reach the purpose of energy-saving and emission-reduction.
(3), the present invention's air of when using work, adding burning by with regenerator in ceramic heat storage body carry out exchange heat, make its temperature rise to 800 ℃ even higher, the flame boundary of the air of high temperature when burning is no longer obvious like this, improve evenly heat intensity, fuel economy and furnace heat transfer efficient in furnace temperature uniformity, the stove, also reduced SO simultaneously
2, NO
xDeng the generation of sour gas, play the function of reduction of discharging.
Four, description of drawings
Fig. 1 is a structural representation of the present invention.
Five, specific embodiment
Further describe the present invention below in conjunction with embodiment:
A kind of as shown in Figure 1 tubular heater, comprise radiation heating chamber 1 and burner 2, radiation heating chamber 1 main body of heater 1.1, furnace chamber 1.2 and boiler tube 1.3 constitute, boiler tube 1.1 is installed in the furnace chamber 1.2, connection two regenerator 3 are installed in body of heater 1.1 outsides, and regenerator 3 comprises outer wall 3.1 and spherical ceramic heat storage 3.2; Be provided with a partition wall 4 in the furnace chamber 1.2 between two regenerator 3, furnace chamber 1.2 be partitioned into left and right two furnace chambers that communicate; Boiler tube 1.1 is along inboard wall of furnace body and the single arrangement of partition wall 4 outer walls; Above Connectivity Section 3.3 that regenerator 3 links to each other with body of heater 1.1 a flame controller 5 is installed, it is a metal drum, and the upper end bucket wall of metal drum has smoke hole 5.1, and the lower end is an open ports 5.2, and combustion flame can be by open ports 5.2 in the metal drum internal combustion; Two regenerator connect a dew point liquid gathering-device 6 respectively; One end of breather pipe 7 links to each other with dew point liquid gathering-device 6, the other end links to each other with 24 direction changeover valves 8, one end of air input pipe 9 and flue gas efferent duct 10 is connected with 24 direction changeover valves 8 respectively, the other end of air input pipe 9 connects air blast or air-introduced machine, and the other end of flue gas efferent duct 10 is communicated to chimney; Burner 2 is installed in regenerator 3 and the Connectivity Section 3.3 that body of heater 1.1 links to each other, and burner 2 links to each other with fuel-supply pipe.
Operation principle of the present invention is: fuel valve 11 and 24 direction changeover valves 8 are under the control of switched system, earlier the fuel valve 11 of right side burner 2 is closed, 11 unlatchings of fuel valve of left side burner 2, air enters in the regenerator 3 in left side through the breather pipe 7 and the dew point liquid gathering-device 6 in 9,24 direction changeover valves 8 of air input pipe, left side simultaneously, spherical ceramic heat storage 3.2 is heated more than 800 ℃, burn with the fuel mix of left side burner 2 ejections, the upper end is in metal drum in its combustion flame again; After metal drum is heated, again boiler tube 1.1 in the left side burner hearth 1.2 is carried out heat radiation, high-temperature flue gas after the burning flows out by smoke hole 5.1 simultaneously, boiler tube 1.1 in the burner hearth 1.2 is carried out heat radiation, and enter right side regenerator 3 from the burner hearth 1.2 on right side, it carries out waste heat and holds receipts by 3.2 pairs of high-temperature flue gas of spherical ceramic heat storage, makes flue-gas temperature be reduced to below 150 ℃ SO in the flue gas
2, NO
xThe dew point lye that produces is by dew point liquid gathering-device 6; Flue gas feeds the chimney discharge through 7,24 direction changeover valves 8 of right side breather pipe and flue gas efferent duct 10 again; By switched system control 24 direction changeover valves 8 are carried out 90 degree rotation commutations after a period of time, the fuel valve of left side burner 2 is closed simultaneously, the fuel valve of right side burner 2 is opened, in the breather pipe 7 on 9,24 direction changeover valves 8 of air process air input pipe, right side and the regenerator 3 that dew point liquid gathering-device 6 enters the right side, spherical ceramic heat storage 3.2 heats it, burn with the fuel mix of right side burner 2 ejections, the upper end is in the metal drum at flame controller 5 in its combustion flame again; After metal drum is heated, again boiler tube 1.1 in the right side burner hearth 1.2 is carried out heat radiation, high-temperature flue gas after the burning flows out by smoke hole 5.1 simultaneously, boiler tube 1.1 in the burner hearth 1.2 is carried out heat radiation, and enter left side regenerator 3 from the burner hearth 1.2 in left side, it carries out waste heat and holds receipts by 3.2 pairs of high-temperature flue gas of spherical ceramic heat storage, makes flue-gas temperature be reduced to below 150 ℃ SO in the flue gas
2, NO
xThe dew point lye that produces is by dew point liquid gathering-device 6; Flue gas feeds the chimney discharge through 7,24 direction changeover valves 8 of left side breather pipe and flue gas efferent duct 10 again; Tubular heater is so alternately running more subsequently.
24 logical commutation cycles of switching rotary valve can be regulated, to reach best burning and heat-transfer effect.Heating furnace is equipped with igniting and automatic temperature control device automatically, can control furnace temperature easily, make easy and simple to handle, the production efficiency height, heating quality is stable, is fit to large-scale continuous production and uses.
Claims (8)
1, a kind of tubular heater, comprise radiation heating chamber (1) and burner (2), radiation heating chamber (1) mainly is made of body of heater (1.1), furnace chamber (1.2) and boiler tube (1.3), boiler tube (1.3) is installed in the furnace chamber (1.2), it is characterized in that in body of heater (1.1) outside connection two regenerator (3) being installed, regenerator (3) comprises outer wall (3.1) and ceramic heat storage body (3.2); Two regenerator (3) link to each other with 24 direction changeover valves (8) by a breather pipe (7) respectively, also are connected with air input pipe (9) and flue gas efferent duct (10) on 24 direction changeover valves (8); Burner (2) is installed in regenerator (3) and the Connectivity Section (3.3) that body of heater (1.1) links to each other.
2, tubular heater according to claim 1 is characterized by in the furnace chamber (1.1) between two regenerator (3) and is provided with more than one partition wall (4), and partition wall (4) is partitioned into two Room or multicell with furnace chamber (1.1), and adjacent two Room communicate.
3, tubular heater according to claim 1 is characterized by in the top of the Connectivity Section (3.3) that regenerator (3) links to each other with body of heater (1.1) a flame controller (5) is installed.
4, tubular heater according to claim 3, it is characterized by flame controller (5) is a metal drum, and the upper end bucket wall of metal drum has smoke hole (5.1), and the lower end is an open ports (5.2).
5, tubular heater according to claim 4, it is characterized by the isometrical or aperture that the metal drum sidewall has closeness up and down and increase has little of big hole.
6,, it is characterized by and on two regenerator (3), be connected and installed with a dew point liquid gathering-device (6) respectively according to claim 1,2,3 or 4 described tubular heaters.
7, tubular heater according to claim 1 is characterized by ceramic heat storage body (3.2) and can be sphere or honeycombed.
8, tubular heater according to claim 1 is characterized by boiler tube and arrange arrangement for coiled pipe more in body of heater (1.1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100197654A CN101251300A (en) | 2008-03-14 | 2008-03-14 | Pipe type heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100197654A CN101251300A (en) | 2008-03-14 | 2008-03-14 | Pipe type heating furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101251300A true CN101251300A (en) | 2008-08-27 |
Family
ID=39954819
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2008100197654A Pending CN101251300A (en) | 2008-03-14 | 2008-03-14 | Pipe type heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101251300A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218526A (en) * | 2011-05-25 | 2011-10-19 | 浙江大学 | High-efficiency and energy-saving roasting device for steel ladles |
| CN103423870A (en) * | 2013-09-02 | 2013-12-04 | 北京华福神雾工业炉有限公司 | Heat accumulation type combustion vacuum phase-change heating furnace |
| CN104279881A (en) * | 2014-10-16 | 2015-01-14 | 刘庆德 | Black smoke treatment device for metal smelting process |
| CN107523324A (en) * | 2017-08-11 | 2017-12-29 | 中国化学工程第六建设有限公司 | Reforming reaction heating furnace is used in oil refining |
-
2008
- 2008-03-14 CN CNA2008100197654A patent/CN101251300A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218526A (en) * | 2011-05-25 | 2011-10-19 | 浙江大学 | High-efficiency and energy-saving roasting device for steel ladles |
| CN103423870A (en) * | 2013-09-02 | 2013-12-04 | 北京华福神雾工业炉有限公司 | Heat accumulation type combustion vacuum phase-change heating furnace |
| CN103423870B (en) * | 2013-09-02 | 2016-08-10 | 洪阳冶化工程科技有限公司 | Heat storage type combustion vacuum phase transition heating furnace |
| CN104279881A (en) * | 2014-10-16 | 2015-01-14 | 刘庆德 | Black smoke treatment device for metal smelting process |
| CN107523324A (en) * | 2017-08-11 | 2017-12-29 | 中国化学工程第六建设有限公司 | Reforming reaction heating furnace is used in oil refining |
| CN107523324B (en) * | 2017-08-11 | 2019-06-11 | 中国化学工程第六建设有限公司 | Oil refining reforming reaction heating furnace |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204514035U (en) | Double heat storage type gas heating furnace | |
| CN201184696Y (en) | Tube type heating stove | |
| CN106705077A (en) | Waste gas incinerator | |
| CN103615905B (en) | Continuous heat accumulation type industrial furnace afterheat utilizing system | |
| CN101251300A (en) | Pipe type heating furnace | |
| CN203489670U (en) | Regenerative type continuous flame tube heating furnace | |
| CN201476597U (en) | Ceramic kiln smoke purifying and surplus heat comprehensive utilization device | |
| CN107559812A (en) | Modular multistage phase-change heat-storage high-temperature air burning energy saver | |
| CN100557329C (en) | A kind of windspout segregated combustion heat-storing tubular oven | |
| CN204739901U (en) | Recuperative heater with circulation canal | |
| CN101545675A (en) | Double fuel gas cycle hot blast stove of waste gas direct combustion and indirect heat transfer | |
| CN201209854Y (en) | Thermal storage type oxygen-enriched combustion apparatus | |
| CN201041352Y (en) | Building block type heat storage and combustion total radiation boiler | |
| CN201508037U (en) | Direct-combustion tube-typed grate organic heat carrier boiler | |
| CN201547957U (en) | Organic thermo carrier boiler | |
| CN2542982Y (en) | Flat-flame coal-fired boiler | |
| CN201449007U (en) | A turn-back flow coal burning hot air furnace | |
| CN205579547U (en) | Low nitrogen buggy organic heat carrier boiler | |
| CN2544226Y (en) | Reverse combustion secondary air vertical multipurpose boiler | |
| CN212805673U (en) | Full-automatic constant-pressure modular waste gas incinerator | |
| CN201522189U (en) | Rotary kiln combustion chamber heating device | |
| CN217559865U (en) | Organic heat carrier furnace burning biomass gas | |
| CN202008151U (en) | Waste gas circulating system for combustion engine | |
| CN203443093U (en) | Hot-water boiler | |
| CN102901269A (en) | Multipurpose direct coal-fired machine for refrigeration, heat supply and bathing |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20080827 |