CN102042609A - Rotary high-temperature air preheater - Google Patents
Rotary high-temperature air preheater Download PDFInfo
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- CN102042609A CN102042609A CN2010106000435A CN201010600043A CN102042609A CN 102042609 A CN102042609 A CN 102042609A CN 2010106000435 A CN2010106000435 A CN 2010106000435A CN 201010600043 A CN201010600043 A CN 201010600043A CN 102042609 A CN102042609 A CN 102042609A
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- loam cake
- air preheater
- temperature air
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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Abstract
The invention provides a rotary high-temperature air preheater which is characterized by comprising an outer frame, wherein a supporting cylinder, a rotor and a transmission gear are arranged in the outer frame; the rotor is positioned on the supporting cylinder; the transmission gear is positioned on one side of the supporting cylinder; the transmission gear is connected with the rotor; the rotor is provided with an upper cover; and the upper cover is connected with the outer frame through an expansion guide. The invention can be quickly assembled, and can allow a furnace with input of about 1200 DEG C to discharge waste gas; and by using the preheater, the temperature of the output hot air can reach about 1000 DEG C to the maximum, and the temperature of the discharged waste gas is reduced to below 200 DEG C.
Description
The application is dividing an application of a kind of rotary high-temperature air preheater, and the applying date of original application is on October 21st, 2009, and application number is: 200910197461.1, and denomination of invention is a kind of rotary high-temperature air preheater.
Technical field
The present invention relates to rotary high-temperature air preheater, the Waste Heat Recovery that is used for various Industrial Stoves, toxic emission temperature can be controlled at below 200 ℃, and the highest air heating-up temperature can reach about 1000 ℃, belong to the rotary type heat exchanger technical field, relate in particular to high-temperature component material.
Background technology
Rotary regenerative air preheater is the mature equipment that generally adopts in the large-sized boiler system, and it utilizes the heat storage (generally claiming rotor) that continues by thermal current and cold airflow, has realized that heat is from the sustained delivery of thermal current to cold airflow.
In the preheater recovery technology field of Industrial Stoves, generally adopt two fixed storage heaters to reclaim the combustion gas heat at present, two storage heater alternations, the interior waste gas of discharging of storage heater by kiln, its inner heat accumulating element absorbs heat; Another storage heater inside is by combustion air simultaneously, and heat accumulating element adds hot-air, brings heat into burner hearth, and two storage heater alternations are finished by a cross valve.The deficiency that this mode exists mainly contains:
(1) hearth combustor needs two covers, confession fuel conduit etc. all needs two covers, invests bigger;
(2) there are obviously pulsation in fire box temperature, pressure, and there is certain difficulty in control of product quality;
(3) combustion control device complexity.
The a large amount of at present metal heat accumulating elements that adopt of rotary regenerative air preheater generally can not bear the operating temperature more than 450 ℃.And adopting ceramic material to make heat storage in the fixed storage heater, operating temperature can reach 1500 ℃.As nonmetal heat accumulating element being used in the swinging heat exchange, to the kiln of combustion gas temperature at 1000-1200 ℃, the heat outputting air themperature can reach about 1000 ℃.
Summary of the invention
The objective of the invention is can the implementation structure quick-assembling, can import kiln combustion gas about 1200 ℃, realize that the output hot blast temperature is up to about 1000 ℃, the combustion gas temperature is reduced to the rotary high-temperature air preheater below 200 ℃.
In order to achieve the above object, technical scheme of the present invention provides a kind of rotary high-temperature air preheater, it is characterized in that, comprise outside framework, the transmission device that is provided with supporting cylinder, is positioned at the rotor on the supporting cylinder and is positioned at supporting cylinder one side in the outside framework, transmission device connects rotor, and rotor is provided with loam cake, and loam cake connects outside framework by expansion guide.
Further, described loam cake comprises the loam cake housing and is located at its inboard loam cake base insulating layer, the edge of loam cake housing upper surface is provided with the sealing gland supply air line, the middle part of loam cake housing upper surface is respectively equipped with kiln waste gas inlet tube and hot-air efferent duct, kiln waste gas inlet tube and hot-air efferent duct are communicated with the heating kiln furnace exhaust district and the hot-air district of loam cake housing downside respectively, are provided with radial seal plate in top between heating kiln furnace exhaust district and the hot-air district.
Described rotor comprises the rotor coverboard, be provided with central tube in the middle of the rotor case intralamellar part, be provided with radially dividing plate between central tube and the rotor coverboard, radially be provided with heat accumulating element between the dividing plate, be provided with rotor coverboard insulation construction between heat accumulating element and the rotor coverboard, radially the dividing plate upside is connected diaphragm seal and lower sealing piece respectively with downside, last diaphragm seal is provided with sealing clamp, the upside of rotor coverboard and downside are respectively equipped with labyrinth end plate and following labyrinth end plate, the downside of following labyrinth end plate is provided with the supporting rail guidance tape, and the lower end, the outside of rotor coverboard is provided with the driving shroud.
Described supporting cylinder comprises cylindrical shell and is located at its inboard inner barrel heat-insulation layer, the cylindrical shell upside is provided with the lower flange end plate, the cylindrical shell downside connects base plate, the centre of inner barrel is provided with bottom radial seal plate, the both sides of inner barrel are communicated with cold air access tube and exhaust emission tube respectively, the cold air access tube is provided with perforate, and the cylindrical shell outer upper end is provided with the load-bearing roller devices.
Described outside framework comprises by what corner post and newel linked together and lands framework and upper frame, corner post and newel be arranged in parallel, newel is located at the position between the adjacent corner post, the newel middle inside is provided with the rotor centralizer, lands the end angle place of framework to be provided with the transmission device gripper shoe.
Described transmission device comprises the reductor base, and the reductor base is provided with reductor, and reductor connects motor, and reductor connects gear.
Integral device operation principle of the present invention is with the heating surface rotary regenerative air preheater in the station boiler systems of a large amount of uses at present, adopt rotor axis to be arranged vertically mode, inner two kinds of fluid countercurrent current flow, kiln waste gas enters from the top, cold air enters from the below, and cold fluid and hot fluid separates with seal area.
Advantage of the present invention is:
(1) realizes continuing to conduct heat, do not need the storage heater switching device shifter;
(2) operation principle mature and reliable;
(3) kiln only needs a cover combustion apparatus, and system is simple, and control is convenient;
(4) kiln internal pressure, temperature substantially constant help improving kiln output products quality;
(5) take up an area of not quite compact conformation;
(6) heat accumulating element is from the horse's mouth, and manufacturer is numerous, and is cheap;
(7) structure is easy to assembly, and is not high to site requirements.
Description of drawings
Fig. 1 is the rotary high-temperature air preheater structural representation;
Fig. 2 is a upper cover top view;
Fig. 3 is the loam cake upward view;
Fig. 4 is the rotor vertical view;
Fig. 5 is the rotor upward view;
Fig. 6 is the supporting cylinder structural representation;
Fig. 7 is outside frame construction schematic diagram;
Fig. 8 is the transmission structures schematic diagram.
The specific embodiment
Specify the present invention below in conjunction with embodiment.
Embodiment
As shown in Figure 1, be the rotary high-temperature air preheater structural representation, described rotary high-temperature air preheater is made up of loam cake 1, rotor 2, supporting cylinder 3, transmission device 4, outside framework 5 and expansion guide 6.The transmission device 4 that is provided with supporting cylinder 3, is positioned at the rotor 2 on the supporting cylinder 3 and is positioned at supporting cylinder 3 one sides in the outside framework 5, transmission device 4 connects rotor 2, and rotor 2 is provided with loam cake 1, and loam cake 1 connects outside framework 5 by expansion guide 6.
As shown in Figure 2, be upper cover top view, Fig. 3 is its upward view, described loam cake 1 comprises loam cake housing 11 and is located at its inboard loam cake base insulating layer 17, the edge of loam cake housing 11 upper surfaces is provided with sealing gland supply air line 15, the middle part of loam cake housing 11 upper surfaces is respectively equipped with kiln waste gas inlet tube 12 and hot-air efferent duct 13, kiln waste gas inlet tube 12 and hot-air efferent duct 13 are communicated with the heating kiln furnace exhaust district 18 and the hot-air district 19 of loam cake housing 11 downsides respectively, are provided with top radial seal plate 16 between heating kiln furnace exhaust district 18 and the hot-air district 19.
As shown in Figure 4, be the rotor vertical view, Fig. 5 is its upward view, described rotor 2 comprises rotor coverboard 28, rotor coverboard 28 bosoms are provided with central tube 21, be provided with radially dividing plate 22 between central tube 21 and the rotor coverboard 28, radially be provided with heat accumulating element 32 between the dividing plate 22, be provided with rotor coverboard insulation construction 29 between heat accumulating element 32 and the rotor coverboard 28, radially dividing plate 22 upsides are connected diaphragm seal 23 and lower sealing piece 25 respectively with downside, last diaphragm seal 23 is provided with sealing clamp 24, the upside of rotor coverboard 28 and downside are respectively equipped with labyrinth end plate 26 and following labyrinth end plate 27, the downside of following labyrinth end plate 27 is provided with supporting rail guidance tape 31, and the lower end, the outside of rotor coverboard 28 is provided with and drives shroud 30.
As shown in Figure 6, be the supporting cylinder structural representation, described supporting cylinder 3 comprises cylindrical shell 35 and is located at its inboard inner barrel heat-insulation layer 38, cylindrical shell 35 upsides are provided with lower flange end plate 36, cylindrical shell 35 downsides connect base plate 39, the centre of cylindrical shell 35 inside is provided with bottom radial seal plate 42, the both sides of cylindrical shell 35 inside are communicated with cold air access tube 41 and exhaust emission tube 40 respectively, cold air access tube 41 is provided with perforate 43 and is used for connecting sealing gland supply air line 15, and cylindrical shell 35 outer upper end are provided with load-bearing roller devices 37.
As shown in Figure 7, be outside frame construction schematic diagram, described outside framework 5 comprises by what corner post 46 and newel 47 linked together and lands framework 45 and upper frame 48, corner post 46 and newel 47 be arranged in parallel, newel 47 is located at the position between the adjacent corner post 46, newel 47 middle inside are provided with rotor centralizer 50, land the end angle place of framework 45 to be provided with transmission device gripper shoe 49.
As shown in Figure 8, be the transmission structures schematic diagram, described transmission device 4 comprises reductor base 54, and reductor base 54 is provided with reductor 52, and reductor 52 connects motor 51, and reductor 52 connects gear 53.
Sealing gland supply air line 15 links to each other with perforate 43, and high-head cold wind introducing upper flange end plate 14 and last labyrinth end plate 26 are constituted the pressurization labyrinth seal structure together, and air-isolation preheater internal heat air and hot waste gas leak in external environment.Loam cake weight is delivered on the outside framework 5 by aligning and the expansion guide 6 that is located at newel 47 tops.Loam cake 1 is used for the enclosed rotor upper space, introduce kiln waste gas and heat outputting air, rotor 2 is used for holding heat accumulating element 32, use as middle heat storage, support cylindrical shell 3 and be used for 2 times side spaces of enclosed rotor, introduce cold air and combustion gas, with effects such as kiln waste gas and cold air after the heat release separate.Be positioned at that labyrinth end plate 27 forms labyrinth seal together under the lower flange end plate 36 that supports cylindrical shell 3 tops and the rotor.Outside framework 5 is used for the weight of the equipment that bears, and lays transmission device 4 etc.Totally 4 groups of rotor centralizer 50() be the centering roller, the excircle of itself and supporting rail guidance tape 31 cooperates, and can keep the axis of operation of rotor 2, avoids rotating sideslip.The gear of transmission device 4 matches with driving shroud 30, drives rotor 2 and rotates.Supporting rail guidance tape 31 matches with load-bearing roller devices 37, realizes the rotation of rotor 2.
Above-mentioned high temperature resistant component material selection is as follows:
The condition of work of this equipment is high temperature, the high kiln waste gas of contact dustiness, and each parts selection principle is:
(1) heat accumulating element 32: heat accumulating element adopts ceramic material, selects ceramic component according to operating temperature, to the equipment of inlet EGT below 1300 ℃, selects for use alumina content at 20%～30% kaolin pottery.Form can be the porcelain ball of diameter 15～30mm, or the ceramic honey comb of hole hydraulic diameter in 3～15mm scope, or the forming process of ceramics sheet accumulation body of voidage in 50～90% scopes.Select which kind of form for use, decide according to the ash content and the impurity situation of kiln combustion gas;
(2) be exposed to more than 450 ℃ construction material in the hot flue gas and air: comprise radially dividing plate 22, central tube 21, top radial seal plate 16, go up diaphragm seal 23, go up sealing clamp 24 etc., adopt anti-1200 ℃ steel 310S, thickness is selected for use according to Strength Calculation and material oxidation speed;
(3) 450 ℃ of following work materials in operating temperature zone: select general carbon steel steel for use, nitriding heat treatment is carried out on roller class surface, and outside framework 5 is selected H shaped steel for use;
(4) insulation material: the filling class is selected the alumina silicate lightweight refracrory of thickness 200-300mm for use, and rotor coverboard insulation construction 29, loam cake base insulating layer 17, inner barrel heat-insulation layer 38 are selected light fire brick for use.Adjacent part adopts the fireproof coating bonding.The air preheating housing external temperature is controlled at and is no more than in 30 ℃ of the environment temperatures.
Hermetically-sealed construction of the present invention is:
(1) upward between labyrinth end plate 26 and the upper flange end plate 14 the pressurization labyrinth seal is set, constitutes labyrinth seal, and introduce the high-head cold wind, cut off internal high temperature gas and in environment, leak by cold air access tube 41 by upper flange end plate 14 and last labyrinth end plate 26;
(2) labyrinth end plate 27 and lower flange end plate 36 constitute labyrinth seal (general road, labyrinth number is no less than 5) down, and the gas that air side spills is harmless cold air, and the combustion gas side is a negative pressure, so waste gas can not spill;
(3) top radial seal plate 16 and last diaphragm seal 23 constitute sealing, can effectively reduce the leakage (but can't fully block) of hot-air to high-temp waste gas; Bottom radial seal plate 42 and lower sealing piece 25 constitute sealing pair, effectively stop the leakage (also can't fully block) of cold air to low temperature waste gas.For reducing leakage rate, top radial seal plate 16 and bottom radial seal plate 42 should be able to cover 1 ~ 2 rotor lattice storehouse fully.The number in rotor lattice storehouse is looked root diameter, and general diameter is arranged 8～18 less than 3.5 meters, and 3.5～6 meters of root diameters are arranged 12～24.
The rotor Calculation of Thermal Deformation is as follows:
Because of adopting the rotor periphery supporting, rotor 2 upper surfaces will form quadratic surface, and central tube 21 place's upthrow amounts are calculated as follows: Δ H=k* Δ T*R*R/(2*h)
Wherein, k: dividing plate expansion of metal coefficient radially, Δ T: dividing plate upper and lower temperature difference radially, R: rotor coverboard radius, h: heat accumulating element height.
Can stay the seal clearance of preheater in view of the above.This outer rotor 2 axially and radially also will have certain linear expansion amount, design labyrinth seal and reserve loam cake 1 and during rotor 2 gaps, determine according to this swell increment.
Transmission power is calculated as follows:
The transmission resistance comprises the frictional resistance moment of diaphragm seal 23 and top radial seal plate 16, lower sealing piece 25 and bottom radial seal plate 42, selects the big person of frictional force (can not take place simultaneously) up and down; And following labyrinth end plate 27 and the 36 formation labyrinth seals of lower flange end plate, upper flange end plate 14 and the last labyrinth end plate 26 formation frictional resistance moments that labyrinth seal produced, the labyrinth seal resistance needs to consider simultaneously up and down.To adopting load-bearing roller devices 37 support patterns, need to calculate the moment of resistance that roller produces.
Rotor speed can be selected the scope of 1～3rpm for use according to the heat exchange property analysis.The safety coefficient of motor 51 and reductor 52 is according to being not less than 1.5 times of considerations.
Heat exchange is calculated as follows:
Adopt compact heat exchanger computer general method.Wherein the convection recuperator coefficient and the resistance coefficient of heat accumulating element 32 need by conducting heat and the wind tunnel test acquisition.Consider that heating surface distributes reasonability, it is comparatively reasonable that exhaust gas side can take 1～3 storehouse lattice than air side more, but for for the purpose of the simplicity of design, waste gas and air side employing symmetric design are more common.
Selection method is as follows:
Generally to be no more than 1.2kPa be foundation to calculate continuous operating condition flue gas resistance, the diameter of selected heat exchanger in view of the above, and the air side availability with air preheater is not less than 85% another control index as type selecting again.Both take all factors into consideration, and finally determine the use amount (immediate shipment raising degree) of rotor 2 diameters and heat accumulating element 32.
As adopt ceramic bead to make heat accumulating element, and need to adjust the fluidizing velocity of ceramic bead, guarantee that the hot air outlet flow velocity is lower than the heat-storing sphere fluidizing velocity, avoid the heat accumulating element layer fluidisation swelling to occur, causing heat-storing sphere is that hot blast is brought the appearance of stove phenomenon into.
The fast-assembling design is as follows:
To the air preheater of diameter below 3.5, can consider to assemble back integral body and dispatch from the factory, transport directly to the erecting bed, work on the spot only for removing the transportation fixed structure and connecting waste gas and air pipe line, is sent work such as electricity to transmission system.
To the big air preheater equipment of 3.5 meters～6 meters of diameters, can make several sections in the manufacturing shop, be transported to on-the-spot back and make up, the main work on the spot of apparatus body is simple assembling and adjusting work, uses facility to be truck crane.
Though the present invention is developed by Industrial Stoves, some technology as the flaky pottery heat accumulating element, also can be used on the large-scale air preheater, thereby promote its high temperature resistant or resistance to corrosion.The quick fixation structure rotary high-temperature air preheater of form of the present invention, use field can be generalized to the industrial furnace of other industry fully, comprise on the equipment such as converter, annealing furnace, calcining furnace, as the waste heat recovery plant of a new generation.
Claims (5)
1. rotary high-temperature air preheater comprises loam cake (1), rotor (2), supports cylindrical shell (3), transmission device (4), outside framework (5), expansion guide (6) and insulation material;
Described rotor (2) comprises rotor coverboard (28), and rotor coverboard 28 bosoms are provided with central tube (21), is provided with radially dividing plate (22) between central tube (21) and the rotor coverboard (28), radially is provided with heat accumulating element (32) between the dividing plate (22); It is characterized in that:
Heat accumulating element (32) adopts ceramic material, selects ceramic component according to operating temperature, to the equipment of inlet EGT below 1300 ℃, selects for use alumina content at 20%～30% kaolin pottery.
2. rotary high-temperature air preheater according to claim 1 is characterized in that,
The porcelain ball that described ceramic material form is diameter 15～30mm, or the ceramic honey comb of hole hydraulic diameter in 3～15mm scope, or the forming process of ceramics sheet accumulation body of voidage in 50～90% scopes.
3. rotary high-temperature air preheater according to claim 1 is characterized in that,
Described radially dividing plate (22) upside is connected diaphragm seal (23) and lower sealing piece (25) respectively with downside, and last diaphragm seal (23) is provided with sealing clamp (24);
Described radially dividing plate (22), central tube (21), last diaphragm seal (23), last sealing clamp (24) adopt anti-1200 ℃ steel 310S.
4. rotary high-temperature air preheater according to claim 1 is characterized in that,
Described loam cake (1) comprises loam cake housing (11), is provided with top radial seal plate (16) between the heating kiln furnace exhaust district (18) of described loam cake housing (11) downside and hot-air district (19);
Top radial seal plate (16) adopts anti-1200 ℃ steel 310S.
5. rotary high-temperature air preheater according to claim 1 is characterized in that,
Described loam cake (1) comprises loam cake housing (11) and is located at its inboard loam cake base insulating layer (17), selects light fire brick for use;
Be provided with rotor coverboard insulation construction (29) between described heat accumulating element (32) and the rotor coverboard (28) and select light fire brick for use;
Described supporting cylinder (3) comprises cylindrical shell (35) and is located at its inboard inner barrel heat-insulation layer (38) and selects light fire brick for use;
Fill the class insulation material and select the alumina silicate lightweight refracrory of thickness 200-300mm for use.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010106000435A CN102042609B (en) | 2009-10-21 | 2009-10-21 | Rotary high-temperature air preheater |
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| CN2010106000435A CN102042609B (en) | 2009-10-21 | 2009-10-21 | Rotary high-temperature air preheater |
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| CN2009101974611A Division CN101761935B (en) | 2009-10-21 | 2009-10-21 | Rotary high-temperature air preheater |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102322745A (en) * | 2011-09-29 | 2012-01-18 | 岳阳钟鼎热工电磁科技有限公司 | Ventilation device for replacing and washing continuously-rotary heat accumulating type preheater ceramic balls |
| CN103939936A (en) * | 2014-04-24 | 2014-07-23 | 燕瑛侠 | Multistage-pair air-sealing-type sealing system set of rotary air pre-heaters |
| CN103940275A (en) * | 2013-01-18 | 2014-07-23 | 北京神雾环境能源科技集团股份有限公司 | Gas heat exchanger and gas heat exchange system with same |
| WO2014110880A1 (en) * | 2013-01-18 | 2014-07-24 | 北京神雾环境能源科技集团股份有限公司 | Gas heat exchanger and gas heat exchange system having same |
| CN106524817A (en) * | 2016-10-27 | 2017-03-22 | 盛春 | Compressed air sealing system and rotary air preheater comprising same |
| CN109520361A (en) * | 2018-12-27 | 2019-03-26 | 无锡方盛换热器股份有限公司 | A kind of efficient rotary type heat exchanger |
| CN109737444A (en) * | 2019-03-19 | 2019-05-10 | 烟台龙源电力技术股份有限公司 | Rotary regenerative air preheater |
| CN111121211A (en) * | 2020-01-15 | 2020-05-08 | 广州市亿加环境科技有限公司 | Single-hole heat exchanger |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| DE4420131C2 (en) * | 1994-06-09 | 1996-11-07 | Jasper Ges Fuer Energiewirtsch | Heat recovery device |
| CN2357312Y (en) * | 1998-11-23 | 2000-01-05 | 吴同钧 | Labyrinth sealer for rotary air preheater |
| CN1169744C (en) * | 2001-01-22 | 2004-10-06 | 宝山钢铁股份有限公司 | Formular and process for preparing heat-accumulating ceramic balls and honeycomb body |
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2009
- 2009-10-21 CN CN2010106000435A patent/CN102042609B/en active Active
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102322745A (en) * | 2011-09-29 | 2012-01-18 | 岳阳钟鼎热工电磁科技有限公司 | Ventilation device for replacing and washing continuously-rotary heat accumulating type preheater ceramic balls |
| CN102322745B (en) * | 2011-09-29 | 2013-04-10 | 岳阳钟鼎热工电磁科技有限公司 | Ventilation device for replacing and washing continuously-rotary heat accumulating type preheater ceramic balls |
| CN103940275A (en) * | 2013-01-18 | 2014-07-23 | 北京神雾环境能源科技集团股份有限公司 | Gas heat exchanger and gas heat exchange system with same |
| WO2014110880A1 (en) * | 2013-01-18 | 2014-07-24 | 北京神雾环境能源科技集团股份有限公司 | Gas heat exchanger and gas heat exchange system having same |
| CN103940275B (en) * | 2013-01-18 | 2017-02-08 | 北京神雾环境能源科技集团股份有限公司 | Gas heat exchanger and gas heat exchange system with same |
| CN103939936A (en) * | 2014-04-24 | 2014-07-23 | 燕瑛侠 | Multistage-pair air-sealing-type sealing system set of rotary air pre-heaters |
| CN103939936B (en) * | 2014-04-24 | 2016-04-06 | 燕守志 | The multistage secondary air sealed sealing system complexes of rotary regenerative air heater |
| CN106524817A (en) * | 2016-10-27 | 2017-03-22 | 盛春 | Compressed air sealing system and rotary air preheater comprising same |
| CN109520361A (en) * | 2018-12-27 | 2019-03-26 | 无锡方盛换热器股份有限公司 | A kind of efficient rotary type heat exchanger |
| CN109737444A (en) * | 2019-03-19 | 2019-05-10 | 烟台龙源电力技术股份有限公司 | Rotary regenerative air preheater |
| CN111121211A (en) * | 2020-01-15 | 2020-05-08 | 广州市亿加环境科技有限公司 | Single-hole heat exchanger |
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| CN102042609B (en) | 2013-03-06 |
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