CN105910080B - One kind spraying rotary steam generator - Google Patents
One kind spraying rotary steam generator Download PDFInfo
- Publication number
- CN105910080B CN105910080B CN201610225227.5A CN201610225227A CN105910080B CN 105910080 B CN105910080 B CN 105910080B CN 201610225227 A CN201610225227 A CN 201610225227A CN 105910080 B CN105910080 B CN 105910080B
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- connecting tube
- bearing
- adpting flange
- chamber
- fin
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
Abstract
The present invention provides a kind of spraying rotary steam generator, including rotating fins chamber, vaporization chamber, I type sound exchanger, condensation-water drain system, II type sound exchangers and heating steam inlet system, rotating fins chamber include fin supervisor and fin groove；Vaporization chamber includes evaporation locular wall, indirect steam outlet, first conduit and spraying system；I type sound exchanger includes connecting tube and belt pulley；Condensation-water drain system includes a concentric reducer, elbow, connecting tube and adpting flange；II type sound exchanger includes a concentric reducer and connecting tube；Heating steam inlet system includes the connecting tube and elbow of relevant connection.Raw water and heat exchanging pipe contact area can be overcome in existing heat exchanger small by the present invention and skewness, and heat transfer coefficient is small, the technical problem such as cause heat exchange efficiency low, improves processing efficiency, and promoting evaporation rate, faster evaporation effect is more preferable, energy-conservation, efficiently, environmental protection.
Description
Technical field
Type of the present invention is related to a kind of steam generator technical field, and the spraying more particularly to a kind of hot fluid heats formula is revolved
Turn steam generator.
Background technology
With people's living standard raising and scientific and technological progress, the row such as closely related pharmacy, food, beverage with human body
Industry hygienic issues constantly improve, steam generator are widely used in going out for the industry ear pipeline such as pharmacy, food, beverage and storage tank
The fields such as bacterium sterilization.Steam generator uses tubular heat exchanger more at present, and earliest tubular heat exchanger is due to no baffling
The effect of plate, shell fluid flow is more steady, causes heat transfer coefficient small, cumbersome to the intervention functions of tubulation reclaimed water.In this base
On plinth, a series of tubular heat exchanger that shell sides are provided with deflection plate, including segmental baffle board heat exchangerses and spiral are developed
Baffle heat exchanger.
Publication No. CN204404134 U patent document discloses a kind of tubular type pure steam generator in upright arrangement, its main body
Including steam tank body and heat exchanger, they are connected by condensed water return duct, in order to prevent tubulation dry combustion method, cause thermal deformation, steam
The water for having certain volume is stored in tank body, in evaporator stops operation, steam tank body has a certain amount of water and do not evaporated, so not
Only so that there is portion of energy loss, and the time length of steam is produced, if often interruption uses, the heat loss of water storage is very huge
Greatly, inadequate energy saving economy.Publication No. CN2844831Y patent document discloses a kind of non-equidistant segmental baffle board heat exchangerses,
Its core is the non-isometric distribution of deflection plate, and it reduces flow pressure drop to a certain extent, improves heat-transfer capability, still
The defects of segmental baffle structure is present itself, flow dead and fluid do not release really to the induced vibration of tube bank.It is public
The number of opening is that CN101706227 patent document discloses a kind of shell-and-tube heat exchanger with un-notched traverse baffles, the baffling of this patent
Although plate reduces pressure drop and heat transfer dead band, improve heat transfer efficiency, slow down the vibration and abrasion of pipe, but it will be general
The fluid of logical segmental baffle board heat exchangerses shell side is not rolled over substantially by changing into the vertical stream along tube bank, convection current through the crossing current of tube bank
Stream acts on.The defects of existing for segmental baffle itself, is developed spiral baffle heat exchanger.Existing spiral baffling
Sheet heat exchanger has two classes, and one kind is using the discontinuous spiral shell that two pieces or polylith are fan-shaped, elliptical plate forms approximate helical curved surface
Baffle heat exchanger is revolved, is exactly that approximation is formed by the sector of polylith quadrant such as publication number CN2655156 patent document
Spiral camber structure；Another kind of is the heat exchanger with continuous helical baffle plates using continuous helical curved surface, such as Publication No.
CN101021394 patent document, it all employs continuous helical deflecting plate in the outer shell side of heat exchanger and middle shell side.Both
Although spiral baffle heat exchanger makes flow of fluid form more reasonable, reduce vibration, the shell-side fluid flow dead of pipe
And flow pressure drop, but because its centrifugal action can cause center uneven with ambient fluid, be not suitable for the heat exchange being relatively large in diameter
Device, and due to immature, the processing difficulties of helical baffles of prior art, and cost is high.
Technical problem be present in above tubular heat exchanger, as tubulation deflection plate flow-disturbing effect under caused vibrations, to row
The damage of pipe, and heating steam increase the heated unequal influence of tubulation under deflection plate effect.In order to avoid heating is steamed
The leakage pollution of vapour, heat exchanger uses dual-tubesheet, but adds processing cost.Spray type steam generator uses mostly at present
Electric heating tube does not almost have as thermal source, hot fluid as the spray type steam generator of heating source, a kind of hot fluid heats formula
Spray type steam generator exploitation it is inevitable.
The content of the invention
For defect present in above-mentioned prior art, the present invention is intended to provide a kind of spraying rotary steam generator, energy
Enough overcome in existing heat exchanger raw water and heat exchanging pipe contact area small and skewness, heat transfer coefficient is small, causes heat exchange to be imitated
The low technical problem of rate.
In order to realize above-mentioned technical purpose, the present invention uses following technical proposals：One kind spraying rotary steam generator, bag
Include rotating fins chamber, vaporization chamber, I type sound exchanger, condensation-water drain system, II type sound exchangers and heating steam inlet
System, it is characterised in that：
The rotating fins chamber includes fin supervisor and fin groove, and fin supervisor is provided with porous, is connected with fin groove
Form heat exchange main body；Described rotating fins chamber one end is connected with I type sound exchangers, and the other end connects with II type sound exchanger
Connect；
The vaporization chamber includes evaporation locular wall, indirect steam outlet, first conduit and spraying system, the vaporization chamber set
It is located at outside rotating fins chamber and keeps sealing；
The I types sound exchanger includes connecting tube and belt pulley, and the belt pulley is located at connection pipe outer wall；
The condensation-water drain system includes a concentric reducer, elbow, the company of the both ends different-diameter coordinated with concentric reducer
Adapter, adpting flange, described connecting tube major diameter one end are connected with adpting flange, the connecting tube other end and concentric reducer one end
Connection, the concentric reducer other end connecting bend；
The II types sound exchanger includes a concentric reducer, the connecting tube of the both ends different-diameter coordinated with concentric reducer,
Described connecting tube minor diameter one end is connected with rotating fins chamber, and connecting tube major diameter one end is connected with heating steam inlet system；
The heating steam inlet system includes the connecting tube and elbow of relevant connection, and the connecting tube is handed over II types sound
Parallel operation connecting tube major diameter one end connects.
Further, the rotating fins chamber also includes adpting flange, jump ring, bearing, axle rotation Glais ring, axle stream wind
Fan, concentric reducer and connecting tube；The fin supervisor is connected with connecting tube, then is connected with concentric reducer, then passes through connecting tube and company
Acting flange connects.
Further, the connecting tube that the fin supervisor is responsible for small 0.333 times of bearing inner race thickness with radius ratio fin connects
Connect.
Further, the vaporization chamber also includes bearing air cover, bearing block, flange and axle rotation Glais ring groove；
The bearing block is connected with flange, and the bearing air cover is connected with bearing block single ended bolt, is positioned to bearing；The flange is provided with
Glais ring groove, the axle rotation Glais ring on rotating fins chamber is installed, vaporization chamber is sealed.
Further, the I types sound exchanger also includes adpting flange, bearing air cover, jump ring, bearing, hole rotation
Glais ring groove, Glais ring seat and concentric reducer；The belt pulley is connected to connection pipe outer wall；Adpting flange close to bearing end passes through
Bearing air cover is connected with the adpting flange of condensation-water drain system, there is washer sealing between adpting flange.
Further, the II types sound exchanger also includes adpting flange, described connecting tube minor diameter one end and rotation
The adpting flange connection of fin chamber, connecting tube major diameter one end pass through bearing air cover and the adpting flange of heating steam inlet system
Connection.
Further, the heating steam inlet system also includes adpting flange, bearing air cover, jump ring, bearing, Kong Yongxuan
Turn Glais ring groove, Glais ring seat, concentric reducer；Rotation Glais ring groove in hole is provided with the Glais ring seat, while bearing is risen solid
It is set for using；Adpting flange close to bearing end is connected by bearing air cover with the adpting flange of fin rotating drum.
Further, the indirect steam outlet is arranged at the top of vaporization chamber.
Compared to prior art, the present invention has the advantages that：
1st, this product uses fin groove, tubulation and expanded joint tube sheet, welding tube sheet one when reducing double tube plate heat exchanger processing
Operation difficulty corresponding to one, improves processing efficiency；
2nd, equal quality water surface area of drop after atomization is the 200- that liquid film surface area is formed through tubulation filming device
1000 times, heat exchange contact area is added, promoting evaporation rate, faster evaporation effect is more preferable；
3rd, the fin chamber of rotation adds the heat transfer coefficient of fin outer wall and droplet；
4th, flabellum can both produce downward wind, can also realize the effect of a part of water fender, and water, vapour are divided
From；
5th, by the frequency of inverter control motor, so as to control motor speed, fin rotating drum speed is made in folding
Line cyclic swing, increase the chaotic intensity of vaporization chamber, augmentation of heat transfer；
6th, spraying directly evaporation has the advantages of energy-conservation, efficient, environmentally friendly；Evaporation efficiency is high, and operating efficiency improves 4-6 times.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is rotating fins cavity configuration schematic diagram of the present invention；
Fig. 3 is cross-sectional view of the rotating fins chamber of the present invention along line A-A；
Fig. 4 is vaporization chamber structural representation of the present invention；
Fig. 5 is I types sound exchanger arrangement schematic diagram of the present invention；
Fig. 6 is condensation-water drain system structure diagram of the present invention；
Fig. 7 is present invention heating steam inlet system structure diagram；
Fig. 8 is II types sound exchanger arrangement schematic diagram of the present invention；
Wherein：
1st, adpting flange, 2, bearing air cover, 3, bearing block, 4, jump ring, 5, bearing, 6, indirect steam outlet, 7, flange, 8,
Axle rotation Glais ring, 9, axle rotation Glais ring groove, 10, aerofoil fan, 11, fin groove, 12, first conduit, 13, belt
Wheel, 14, hole rotation Glais ring, 15, hole rotation Glais ring groove, 16, Glais ring seat, 17, concentric reducer, 18, connecting tube, 19,
Elbow, 20, vaporization chamber, 21, fin supervisor, 22, evaporation locular wall, 23, spraying system.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings.
Shown in reference picture 1 and Fig. 6, the utility model provides a kind of spraying rotary steam generator, including rotating fins chamber,
Vaporization chamber, I type sound exchanger, condensation-water drain system, II type sound exchangers and heating steam inlet system.The rotation
Fin chamber includes fin supervisor 21 and fin groove 11, and the fin supervisor 21 is provided with porous, and formation be connected with fin groove 11 and is exchanged heat
Main body；Described rotating fins chamber one end is connected with I type sound exchangers, and the other end is connected with II type sound exchangers；The steaming
Hair room includes evaporation locular wall 22, indirect steam outlet 6, first conduit 12 and spraying system 23, the vaporization chamber and is set in rotation
Turn outside fin chamber and keep sealing；The I types sound exchanger includes connecting tube 18 and belt pulley 13, and the belt pulley 13 is located at
The outer wall of connecting tube 18；The condensation-water drain system includes the both ends of a concentric reducer 17, elbow 19 and the cooperation of concentric reducer 17 not
Connecting tube 18, adpting flange 1 with diameter, described major diameter one end of connecting tube 18 are connected with adpting flange 1, the connecting tube 18
The other end is connected with the one end of concentric reducer 17, the other end connecting bend 19 of concentric reducer 17；The II types sound exchanger includes
One concentric reducer 17, with concentric reducer 17 coordinate both ends different-diameter connecting tube 18, described minor diameter one end of connecting tube 18 with
Rotating fins chamber is connected, and the major diameter one end of connecting tube 18 is connected with heating steam inlet system；The heating steam inlet system
Connecting tube 18 and elbow 19 including relevant connection, the connecting tube 18 and the major diameter one end of II type sound exchangers connecting tube 18
Connection.
Heating steam is entered into rotating fins intracavitary by steam inlet, internally in the presence of component, forms turbulent flow,
Heat exchange is carried out with fin, fin temperature is increased, a part of heat of fin outer wall is delivered to vaporization chamber by convection action, to fortune
Dynamic water droplet is conducted heat, and most of heat is directly exchanged heat with the water droplet group impinged upon in fin, evaporates drop phase transformation,
Produce indirect steam.The rotation of fin chamber promotes the effect that is uniform, increasing thermal convection current that exchanges heat, and destroys the motion structure of water droplet group,
Increase the heat transfer coefficient of water and fin outer wall；Aerofoil fan produces downward wind-force, increase to the fluid domain between adjacent fins
Run duration and air-flow confusion degree of the drop in vaporization chamber, while also have certain facilitation to water, vapour separation；Fin
Rotating drum is connected by flange with being welded with the sound exchanger of belt wheel, and belt wheel is connected work with motor pulley, passes through frequency converter
The frequency of motor is controlled, controls rotating speed, it is in broken line cyclic swing to make fin rotating drum speed, and the confusion for increasing vaporization chamber is strong
Degree, augmentation of heat transfer；Raw water is sent to multiple sprayers by water pump, and sprayer atomizes water into fine liquid particles group, equal quality
Water surface area of drop after atomization is 200-1000 times that liquid film surface area is formed through tubulation filming device, increases heat exchange area；
Due to the drop diameter very little after atomization, the heat required for phase transformation evaporation is few, can accelerate evaporation speed with flash evapn substantially
Degree, while can also produce high-purity indirect steam.
Shown in reference picture 1, Fig. 2 and Fig. 3, as preferably embodiment, the rotating fins chamber is by adpting flange 1, card
Spring 4, bearing 5, axle rotation Glais ring 8, aerofoil fan 10, fin groove 11, concentric reducer 17, connecting tube 18, fin are responsible for 21 groups
Into.Fin supervisor 21 be provided with it is porous, with fin groove 11 weld formed heat exchange main body；Fin supervisor 21 and radius ratio fin supervisor 21
The connecting tube 18 of small 0.333 times of bearing inner race thickness connects, then is welded with concentric reducer 17, finally by connecting tube 18 and connection method
Orchid welding, aerofoil fan are welded on fin supervisor 21.Rotating fins chamber one end passes through adpting flange 1 and I type sound exchangers
The bolt connection of adpting flange 1, the other end and II type sound exchanger bolt connections.The flange 7 of rotating fins chamber and vaporization chamber,
Axle ensures sealing with the cooperation of rotation Glais ring 8.In order to obtain similar technique effect, axle rotation Glais ring 8 can use it
He substitutes high temperature high voltage resistant axle use/hole sealing ring.
Shown in reference picture 1 and Fig. 4, as preferably embodiment, the vaporization chamber is by bearing air cover 2, bearing block 3, and two
Secondary steam (vapor) outlet 6, flange 7, axle rotation Glais ring groove 9, first conduit 12, locular wall 22 is evaporated, spraying system 23 forms.Axle
Bearing 3 is welded with flange 7, and bearing air cover 2 is connected with the single ended bolt of bearing block 3, is positioned to bearing.Flange 7 is provided with axle rotation
Glais ring groove 9, the axle rotation Glais ring 8 on rotating fins chamber is installed, vaporization chamber is sealed.
Shown in reference picture 1 and Fig. 5, as preferably embodiment, the I types sound exchanger is by adpting flange 1, bearing
Transparent cover 2, jump ring 4, bearing 5, belt pulley 13, hole rotation Glais ring groove 15, Glais ring seat 16, concentric reducer 17,18 groups of connecting tube
Into.Glais ring seat 16 can both rotate Glais ring groove 15 with mounting hole, while also play fixation to bearing；Belt pulley 13 is direct
It is welded on the outer wall of connecting tube 18；After pipeline is welded, bearing air cover 2, fixed circlip 4 are first installed, then bearing 5 is installed, finally
Weld Glais ring seat 16；Adpting flange 1 close to bearing end is connected by the bolt of adpting flange 1 of bearing air cover 2 and outlet system
Connect, there is washer sealing between flange.
Shown in reference picture 1 and Fig. 8, as preferably embodiment, the II types sound exchanger is by a concentric reducer 17
It is welded to form with two matched different-diameter connecting tubes 18 with adpting flange 1.Minor diameter flange is connected with rotating fins chamber
The bolt connection of flange 1, major diameter adpting flange 1 are connected by bearing air cover 2 and the bolt of heating steam inlet system adpting flange 1
Connect.
Shown in reference picture 1 and Fig. 7, as preferably embodiment, the heating steam inlet system by adpting flange 1,
Bearing air cover 2, jump ring 4, bearing 5, hole rotation Glais ring groove 15, Glais ring seat 16, concentric reducer 17, connecting tube 18, elbow 19
Composition.Glais ring seat 16 both can rotate Glais ring 15 with mounting hole, while also play fixation to bearing 5, close to bearing end
Adpting flange 1 pass through the bolt connection of adpting flange 1 of bearing air cover 2 and fin rotating drum.
As preferably embodiment, the indirect steam outlet 6 is arranged at the top of vaporization chamber.
The course of work：
Raw water is sent to multiple micro- spray painting days with fog by water pump, and micro- spray painting day with fog atomizes water into fine liquid particles group, on an equal basis
Quality water surface area of drop after atomization is 200-1000 times that liquid film surface area is formed through tubulation filming device, increases heat-transfer surface
Product.Due to the drop diameter very little after atomization, the heat required for each water droplet phase transformation evaporation is few, substantially can with flash evapn,
Evaporation rate is accelerated, while can also produce high-purity indirect steam.Steam is heated to be handed over through II types sound by heating vapour system
Parallel operation enters rotating fins intracavitary, internally in the presence of component, forms turbulent flow, carries out heat exchange with fin, makes fin
Temperature rises, and a part of heat of fin outer wall is delivered to vaporization chamber by the convection action of vapor, and the water droplet group of motion is carried out
Heat transfer, most of heat are directly exchanged heat with impinging upon the water droplet group of fin, evaporate drop phase transformation, produce indirect steam.
It is in broken line mechanical periodicity that motor changes rotating speed under Frequency Converter Control, and I type sound exchangers are delivered in the presence of belt wheel
On belt wheel, the rotation of fin chamber is driven, plays a part of promoting uniform, the increase thermal convection current that exchanges heat, to increase vaporization chamber air-flow
Chaotic intensity, augmentation of heat transfer, the motion structure of destruction water droplet group, the heat transfer coefficient of increase water and fin outer wall.Aerofoil fan pair
Fluid domain between adjacent fins produces downward wind-force, adds run duration and air-flow confusion journey of the drop in vaporization chamber
Degree, while further promote water, the effect of vapour separation.
Instrument described above is the preferred embodiment of the present invention, and instrument is not confined to above-mentioned implementation to protection scope of the present invention
Example, all technical schemes belonged under thinking of the present invention belong to protection scope of the present invention.It should be pointed out that for the art
Those of ordinary skill for, some improvements and modifications without departing from the principles of the present invention, these improvements and modifications
It should be regarded as protection scope of the present invention.
Claims (6)
1. one kind spraying rotary steam generator, including rotating fins chamber, vaporization chamber, I type sound exchanger, condensation-water drain system
System, II type sound exchangers and heating steam inlet system, it is characterised in that：
The rotating fins chamber includes fin supervisor (21) and fin groove (11), the fin be responsible for (21) be provided with it is porous, with wing
Film trap (11) connection forms heat exchange main body；Described rotating fins chamber one end is connected with I type sound exchangers, and the other end moves with II types
Quiet exchanger connection；
The vaporization chamber includes evaporation locular wall (22), indirect steam outlet (6), first conduit (12) and spraying system (23),
The vaporization chamber is set in outside rotating fins chamber and keeps sealing；
The I types sound exchanger includes connecting tube (18) and belt pulley (13), and the belt pulley (13) is located at connecting tube (18)
Outer wall；
The condensation-water drain system include a concentric reducer (17), elbow (19), with concentric reducer (17) cooperation both ends it is different
The connecting tube (18) of diameter, adpting flange (1), described connecting tube (18) major diameter one end are connected with adpting flange (1), the company
Adapter (18) other end is connected with concentric reducer (17) one end, concentric reducer (17) other end connecting bend (19)；
The II types sound exchanger includes the connection of a concentric reducer (17), the both ends different-diameter coordinated with concentric reducer (17)
Manage (18), described connecting tube (18) minor diameter one end is connected with rotating fins chamber, and connecting tube (18) major diameter one end is steamed with heating
Vapour gas handling system connects；
The heating steam inlet system includes the connecting tube (18) and elbow (19) of relevant connection, the connecting tube (18) and II
Type sound exchanger connecting tube (18) major diameter one end connects.
A kind of 2. spraying rotary steam generator according to claim 1, it is characterised in that：The rotating fins chamber also wraps
Include adpting flange (1), jump ring (4), bearing (5), axle rotation Glais ring (8), aerofoil fan (10), concentric reducer (17) and connection
Manage (18)；The fin supervisor (21) is connected with connecting tube (18), then is connected with concentric reducer (17), then passes through connecting tube (18)
It is connected with adpting flange (1)；The vaporization chamber also includes bearing air cover (2), bearing block (3), flange (7) and axle rotation
Glais ring groove (9)；The bearing block (3) is connected with flange (7), and the bearing air cover (2) connects with bearing block (3) single ended bolt
Connect, positioned to bearing；The flange (7) is provided with Glais ring groove, installs the axle rotation Glais ring (8) on rotating fins chamber, right
Vaporization chamber seals.
3. spraying rotary steam generator according to claim 2, it is characterised in that：The fin supervisor (21) and radius
Than connecting tube (18) connection of fin supervisor's (21) small 0.333 times of bearing inner race thickness.
A kind of 4. spraying rotary steam generator according to claim 2, it is characterised in that：The I types sound exchanger
Also include adpting flange (1), bearing air cover (2), jump ring (4), bearing (5), hole rotation Glais ring groove (15), Glais ring seat
(16) it is welded on concentric reducer (17), Glais ring seat (16) on bearing air cover (2), hole rotation Glais ring groove (15) can be arranged on
In Glais ring seat (16)；The belt pulley (13) is connected to connecting tube (18) outer wall；Concentric reducer (17) and it is matched neither
Welded with diameter connecting tube (18) and adpting flange (1), close to bearing end (5) adpting flange (1) by bearing air cover (2) with
The adpting flange (1) of condensation-water drain system connects, and has washer sealing, the heating steam inlet system between adpting flange (1)
System also includes adpting flange (1), bearing air cover (2), jump ring (4), bearing (5), hole rotation Glais ring groove (15), Glais ring seat
(16), concentric reducer (17)；Hole rotation Glais ring groove (15) is provided with the Glais ring seat (16), while bearing (5) is risen solid
It is set for using；Adpting flange (1) close to bearing (5) end is connected by the adpting flange (1) of bearing air cover (2) and fin rotating drum
Connect.
A kind of 5. spraying rotary steam generator according to claim 4, it is characterised in that：The II types sound exchanger
Also include adpting flange (1), described connecting tube (18) minor diameter one end is connected with the adpting flange (1) of rotating fins chamber, connection
Pipe (18) major diameter one end is connected by bearing air cover (2) with heating the adpting flange (1) of steam inlet system.
6. spraying rotary steam generator according to claim 1, it is characterised in that：Indirect steam outlet (6) peace
At the top of vaporization chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610225227.5A CN105910080B (en) | 2016-04-13 | 2016-04-13 | One kind spraying rotary steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610225227.5A CN105910080B (en) | 2016-04-13 | 2016-04-13 | One kind spraying rotary steam generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105910080A CN105910080A (en) | 2016-08-31 |
| CN105910080B true CN105910080B (en) | 2018-01-19 |
Family
ID=56745966
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610225227.5A Active CN105910080B (en) | 2016-04-13 | 2016-04-13 | One kind spraying rotary steam generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105910080B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113648945B (en) * | 2021-08-13 | 2023-04-07 | 浙江工业大学 | Regulation and control method of device capable of achieving sufficient heating and temperature rise of micro-droplets |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004020095A (en) * | 2002-06-18 | 2004-01-22 | Isamu Tekkosho:Kk | Multi-tube type heat transfer agitating device |
| WO2004068054A1 (en) * | 2003-01-31 | 2004-08-12 | Energy Saving Concepts Limited | Heat exchanger |
| CN2655156Y (en) * | 2003-10-30 | 2004-11-10 | 中国石化集团齐鲁石油化工公司 | Screw baffle pipe case type heat exchanger |
| CN2844831Y (en) * | 2005-10-28 | 2006-12-06 | 中油抚顺工程建设有限公司 | Non-equidistant segmental baffle board heat exchangers |
| CN101762203A (en) * | 2008-12-23 | 2010-06-30 | 北京化工大学 | Inner boundary layer cutting disturbing radial mixed flow device of heat exchange pipe |
-
2016
- 2016-04-13 CN CN201610225227.5A patent/CN105910080B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004020095A (en) * | 2002-06-18 | 2004-01-22 | Isamu Tekkosho:Kk | Multi-tube type heat transfer agitating device |
| WO2004068054A1 (en) * | 2003-01-31 | 2004-08-12 | Energy Saving Concepts Limited | Heat exchanger |
| CN2655156Y (en) * | 2003-10-30 | 2004-11-10 | 中国石化集团齐鲁石油化工公司 | Screw baffle pipe case type heat exchanger |
| CN2844831Y (en) * | 2005-10-28 | 2006-12-06 | 中油抚顺工程建设有限公司 | Non-equidistant segmental baffle board heat exchangers |
| CN101762203A (en) * | 2008-12-23 | 2010-06-30 | 北京化工大学 | Inner boundary layer cutting disturbing radial mixed flow device of heat exchange pipe |
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| Publication number | Publication date |
|---|---|
| CN105910080A (en) | 2016-08-31 |
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