CN105910080A - Mist-spray rotary steam generator - Google Patents
Mist-spray rotary steam generator Download PDFInfo
- Publication number
- CN105910080A CN105910080A CN201610225227.5A CN201610225227A CN105910080A CN 105910080 A CN105910080 A CN 105910080A CN 201610225227 A CN201610225227 A CN 201610225227A CN 105910080 A CN105910080 A CN 105910080A
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- China
- Prior art keywords
- connecting tube
- bearing
- fin
- chamber
- adpting flange
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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 invention provides a mist-spray rotary steam generator which comprises a rotary fin chamber, an evaporation room, an I-type dynamic-static exchanger, a condensate water outlet system, an II-type dynamic-static exchanger and a heated steam inlet system, wherein the rotary fin chamber comprises a fin main tube and a fin trough; the evaporation room comprises an evaporation room wall, a secondary steam outlet, a residual water outlet and a mist spray system; the I-type dynamic-static exchanger comprises a connecting tube and a belt wheel; the condensate outlet system comprises a concentric reducer, a bending head, a connecting tube and a connecting flange; the II-type dynamic-static exchanger comprises a concentric reducer and a connecting tube; and the heated steam inlet system comprises a connecting tube and a bending head which form a correlated connection. The mist-spray rotary steam generator provided by the invention solves the technical problems in an existing heat exchanger that a contact area between raw material water and heat exchange row rubes is small and contact is uneven; and a heat transfer coefficient is small and thus heat exchange efficiency is low, etc. The mist-spray rotary steam generator has the advantages that processing efficiency is increased; evaporation is accelerated; evaporation effects are better; and the steam generator is energy-saving, efficient and environment-friendly.
Description
Technical field
Type of the present invention relates to a kind of steam generator technical field, particularly relates to the spraying rotary steam generator of a kind of hot fluid heats formula.
Background technology
Along with people's living standard improves and scientific and technological progress, the professional hygiene problems such as pharmacy closely-related with human body, food, beverage are the most perfect, and steam generator is widely used in the fields such as the sterilization of the industry ear pipelines such as pharmacy, food, beverage and storage tank.Steam generator many employings tubular heat exchanger at present, tubular heat exchanger the earliest is not owing to having the effect of deflection plate, and shell fluid flow is relatively more steady, causes heat transfer coefficient little, cumbersome to the intervention functions of water in tubulation.On this basis, it is developed a series of shell side and the tubular heat exchanger of deflection plate is installed, including segmental baffle board heat exchangers and spiral baffle heat exchanger.
The patent documentation of Publication No. CN204404134 U discloses a kind of tubular type pure steam generator in upright arrangement, its main body includes 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 tank body stores and has the water of certain volume, when evaporator stops operation, there is a certain amount of water and do not evaporate in steam tank body, the most not only make portion of energy lose, and the time producing steam is long, if being often interrupted use, the heat loss of water-retention is the hugest, inadequate energy saving economy.The patent documentation of Publication No. CN2844831Y discloses a kind of non-equidistant segmental baffle board heat exchangers, its core is the non-isometric distribution of deflection plate, it reduces flow pressure drop to a certain extent, improve heat-transfer capability, but the most real releasing of induced vibration that the defect that segmental baffle structure self exists, flow dead and fluid are to tube bank.The patent documentation of Publication No. CN101706227 discloses a kind of shell-and-tube heat exchanger with un-notched traverse baffles, although the deflection plate of this patent reduces pressure drop and heat transfer dead band, improve heat transfer efficiency, slow down vibration and the abrasion of pipe, but the fluid of common segmental baffle board heat exchangers shell side is changed into the vertical stream along tube bank by the crossing current through tube bank by it, and convection current does not has baffling effect substantially.The defect existed for segmental baffle self, is developed spiral baffle heat exchanger.Existing spiral baffle heat exchanger has two classes, one class is to use two pieces or polylith sector, the discontinuous spiral baffle heat exchanger of elliptical plate composition approximate helical curved surface, patent documentation such as publication number CN2655156, it is simply that by the fan-shaped spiral camber structure forming approximation of polylith quadrant；The another kind of heat exchanger with continuous helical baffle plates being to use continuous helical curved surface, such as the patent documentation of Publication No. CN101021394, it all have employed continuous helical deflecting plate at outer shell side and the middle shell side of heat exchanger.Although both spiral baffle heat exchangers make fluid liquid form more reasonable, decrease the vibration of pipe, shell-side fluid flow dead and flow pressure drop, but owing to its centrifugal action can cause center uneven with ambient fluid, be not suitable for the heat exchanger being relatively large in diameter, and immature due to prior art, the processing difficulties of helical baffles, and cost is high.
All there is technical problem in above tubular heat exchanger, the vibrations produced under deflection plate flow-disturbing effect such as tubulation, the damage to tubulation, and add vapours and increase the unequal impact that tubulation is heated under deflection plate effect.Polluting in order to avoid adding the leakage of vapours, heat exchanger uses dual-tubesheet, but adds processing cost.At present spray type steam generator mostly use electric heating tube as thermal source, hot fluid as heating source spray type steam generator almost without, the exploitation of the spray type steam generator of a kind of hot fluid heats formula is inevitable.
Summary of the invention
For defect present in above-mentioned prior art, it is desirable to provide a kind of spraying rotary steam generator, it is possible to overcoming raw water in existing heat exchanger little with heat exchanging pipe contact area and skewness, heat transfer coefficient is little, causes the technical problems such as heat exchange efficiency is low.
In order to realize above-mentioned technical purpose, the present invention uses following technical proposals: a kind of spraying rotary steam generator, including rotating fins chamber, vaporization chamber, I type sound exchanger, condensation-water drain system, II type sound exchanger and heating steam inlet system, it is characterised in that:
Described rotating fins chamber includes that fin supervisor and fin groove, described fin supervisor have porous, is connected formation heat exchange main body with fin groove；One end, described rotating fins chamber is connected with I type sound exchanger, and the other end is connected with II type sound exchanger；
Described vaporization chamber includes evaporating locular wall, indirect steam outlet, first conduit and spraying system, and described vaporization chamber is set in outside rotating fins chamber and keeps sealing；
Described I type sound exchanger includes that connecting tube and belt pulley, described belt pulley are located at connecting tube outer wall；
Described condensation-water drain system includes the connecting tube of two ends different-diameter, the adpting flange that a concentric reducer, elbow coordinate with concentric reducer, described connecting tube major diameter one end is connected with adpting flange, the described connecting tube other end is connected with concentric reducer one end, described concentric reducer other end connecting bend；
Described II type sound exchanger includes the connecting tube of the two ends different-diameter that a concentric reducer coordinates with concentric reducer, and 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；
Described heating steam inlet system includes that connecting tube and the elbow of relevant connection, described connecting tube are connected with II type sound exchanger connecting tube major diameter one end.
Further, described rotating fins chamber also includes that adpting flange, jump ring, bearing, axle rotate Glais ring, aerofoil fan, concentric reducer and connecting tube；Described fin supervisor be connected with connecting tube, then is connected with concentric reducer, is then connected with adpting flange by connecting tube.
Further, the connecting tube that described fin supervisor is responsible for little 0.333 times of bearing inner race thickness with radius ratio fin is connected.
Further, described vaporization chamber also includes that bearing air cover, bearing block, flange and axle rotate Glais ring groove；Described bearing block and Flange joint, described bearing air cover is connected with bearing block single ended bolt, positions to bearing；Described flange has Glais ring groove, installs the axle rotation Glais ring on rotating fins chamber, seals vaporization chamber.
Further, described I type sound exchanger also includes that adpting flange, bearing air cover, jump ring, bearing, hole rotate Glais ring groove, Glais ring seat and concentric reducer；Described belt pulley is connected to connecting tube outer wall；Adpting flange near bearing end is connected with the adpting flange of condensation-water drain system by bearing air cover, has washer sealing between adpting flange.
Further, described II type sound exchanger also includes that adpting flange, described connecting tube minor diameter one end are connected with the adpting flange in rotating fins chamber, and connecting tube major diameter one end is connected by the adpting flange of bearing air cover with heating steam inlet system.
Further, described heating steam inlet system also includes that adpting flange, bearing air cover, jump ring, bearing, hole rotate Glais ring groove, Glais ring seat, concentric reducer；Have hole on described Glais ring seat and rotate Glais ring groove, bearing is played fixation simultaneously；Adpting flange near bearing end is connected with the adpting flange of fin rotating drum by bearing air cover.
Further, the outlet of described indirect steam is arranged on vaporization chamber top.
Compared to prior art, there is advantages that
1, this product use fin groove, reduce double tube plate heat exchanger add man-hour tubulation with expanded joint tube sheet, weld tube sheet operation easier one to one, improve working (machining) efficiency；
2, equal quality water surface area of drop after atomization is form liquid film surface area through tubulation filming device 200-1000 times, adds heat exchange contact area, promotes evaporation rate faster, and evaporation effect is more preferable；
3, the fin chamber rotated adds the heat transfer coefficient of fin outer wall and droplet；
4, flabellum both can produce downward wind, it is also possible to realizes the effect of a part of water fender, separates water, vapour；
5, by the frequency of inverter control motor, thus controlling motor speed, making fin rotating drum speed is broken line cyclic swing, increases the chaotic intensity of vaporization chamber, augmentation of heat transfer；
6, spraying direct evaporation has energy-conservation, efficient, the advantage of environmental protection；Evaporation efficiency is high, and work efficiency improves 4-6 times.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram；
Fig. 2 is rotating fins cavity configuration schematic diagram of the present invention；
Fig. 3 is the rotating fins chamber of the present invention cross-sectional view along line A-A；
Fig. 4 is vaporization chamber structural representation of the present invention；
Fig. 5 is I type sound exchanger arrangement schematic diagram of the present invention；
Fig. 6 is condensation-water drain system structure schematic diagram of the present invention；
Fig. 7 is that the present invention heats steam inlet system structure schematic diagram；
Fig. 8 is II type sound exchanger arrangement schematic diagram of the present invention；
Wherein:
1, adpting flange, 2, bearing air cover, 3, bearing block, 4, jump ring, 5, bearing, 6, indirect steam outlet, 7, flange, 8, axle is with rotating Glais ring, 9, axle is with rotating Glais ring groove, and 10, aerofoil fan, 11, fin groove, 12, first conduit, 13, belt pulley, 14, hole with rotating Glais ring, 15, hole with rotating 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.
Detailed description of the invention
The invention will be further described below in conjunction with the accompanying drawings.
With reference to shown in Fig. 1 and Fig. 6, 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 exchanger and heating steam inlet system.Described rotating fins chamber includes that fin supervisor 21 and fin groove 11, described fin supervisor 21 have porous, is connected formation heat exchange main body with fin groove 11；One end, described rotating fins chamber is connected with I type sound exchanger, and the other end is connected with II type sound exchanger；Described vaporization chamber includes evaporating locular wall 22, indirect steam outlet 6, first conduit 12 and spraying system 23, and described vaporization chamber is set in outside rotating fins chamber and keeps sealing；Described I type sound exchanger includes that connecting tube 18 and belt pulley 13, described belt pulley 13 are located at connecting tube 18 outer wall；Described condensation-water drain system includes the connecting tube 18 of two ends different-diameter, the adpting flange 1 that a concentric reducer 17, elbow 19 coordinate with concentric reducer 17, described connecting tube 18 major diameter one end is connected with adpting flange 1, described connecting tube 18 other end is connected with concentric reducer 17 one end, described concentric reducer 17 other end connecting bend 19；Described II type sound exchanger includes the connecting tube 18 of the two ends different-diameter that a concentric reducer 17 coordinates with concentric reducer 17, and described connecting tube 18 minor diameter one end is connected with rotating fins chamber, and connecting tube 18 major diameter one end is connected with heating steam inlet system；Described heating steam inlet system includes that connecting tube 18 and the elbow 19 of relevant connection, described connecting tube 18 are connected with II type sound exchanger connecting tube 18 major diameter one end.
Vapours will be added and entered rotating fins intracavity by steam inlet, under the effect of internals, form turbulent flow, carrying out heat exchange with fin, make fin temperature increase, a part of heat of fin outer wall is delivered to vaporization chamber by convection action, the water droplet of motion is conducted heat, major part heat directly carries out heat exchange with the water droplet group impinged upon at fin, makes drop phase transformation evaporate, and produces indirect steam.The rotation in fin chamber promotes the effect that heat exchange is uniform, increase thermal convection current, destroys the motion structure of water droplet group, increases the heat transfer coefficient of water and fin outer wall；Aerofoil fan produces downward wind-force to the fluid domain between adjacent fins, adds drop in the movement time of vaporization chamber and air-flow confusion degree, the most also to water, vapour separates certain facilitation；Fin rotating drum is connected with the sound exchanger being welded with belt wheel by flange, and belt wheel is connected work with motor pulley, by the frequency of inverter control motor, control rotating speed, making fin rotating drum speed is broken line cyclic swing, increases the chaotic intensity of vaporization chamber, augmentation of heat transfer；Raw water delivers to multiple aerosol apparatus by water pump, and aerosol apparatus atomizes water into fine liquid particles group, and equal quality water surface area of drop after atomization is form liquid film surface area through tubulation filming device 200-1000 times, increases heat exchange area；Owing to the drop diameter after atomization is the least, the heat required for phase transformation evaporation is few, substantially can accelerate evaporation rate with flash evapn, also can produce high-purity indirect steam simultaneously.
With reference to shown in Fig. 1, Fig. 2 and Fig. 3, as preferably embodiment, described rotating fins chamber is by adpting flange 1, jump ring 4, bearing 5, and axle is with rotating Glais ring 8, and aerofoil fan 10, fin groove 11, concentric reducer 17, connecting tube 18, fin supervisor 21 forms.Fin supervisor 21 has porous, welds formation heat exchange main body with fin groove 11；Fin is responsible for 21 connecting tubes 18 being responsible for 21 little 0.333 times of bearing inner race thickness with radius ratio fin and is connected, then welds with concentric reducer 17, welds with adpting flange finally by connecting tube 18, and aerofoil fan is welded on fin supervisor 21.One end, rotating fins chamber is connected with I type sound exchanger adpting flange 1 bolt by adpting flange 1, and the other end is connected with II type sound exchanger bolt.Rotating fins chamber and the flange 7 of vaporization chamber, seal in axle guarantee under the cooperation rotating Glais ring 8.In order to obtain similar technique effect, axle rotates Glais ring 8 and can substitute with other high temperature high voltage resistant axles/hole sealing ring.
With reference to shown in Fig. 1 and Fig. 4, as preferably embodiment, described vaporization chamber is by bearing air cover 2, bearing block 3, indirect steam outlet 6, flange 7, and axle is with rotating Glais ring groove 9, and first conduit 12, evaporation locular wall 22, spraying system 23 forms.Bearing block 3 welds with flange 7, and bearing air cover 2 is connected with bearing block 3 single ended bolt, positions to bearing.Flange 7 has axle and rotates Glais ring groove 9, installs the axle rotation Glais ring 8 on rotating fins chamber, seals vaporization chamber.
With reference to shown in Fig. 1 and Fig. 5, as preferably embodiment, described I type sound exchanger is by adpting flange 1, bearing air cover 2, jump ring 4, bearing 5, belt pulley 13, and hole is with rotating Glais ring groove 15, and Glais ring seat 16, concentric reducer 17, connecting tube 18 forms.Glais ring seat 16 both can rotate Glais ring groove 15 with installing hole, also bearing is played fixation simultaneously；Belt pulley 13 is directly welded at connecting tube 18 outer wall；After pipeline is welded, bearing air cover 2, fixing jump ring 4 are first installed, then bearing 5 is installed, finally welding Glais ring seat 16；Adpting flange 1 near bearing end is connected with adpting flange 1 bolt of outlet system by bearing air cover 2, has washer sealing between flange.
With reference to shown in Fig. 1 and Fig. 8, as preferably embodiment, described II type sound exchanger is welded to form with adpting flange 1 by a concentric reducer 17 and two matched different-diameter connecting tubes 18.Minor diameter flange is connected with rotating fins chamber adpting flange 1 bolt, and major diameter adpting flange 1 is connected with heating steam inlet system adpting flange 1 bolt by bearing air cover 2.
With reference to shown in Fig. 1 and Fig. 7, as preferably embodiment, described heating steam inlet system is by adpting flange 1, bearing air cover 2, jump ring 4, bearing 5, and hole is with rotating Glais ring groove 15, and Glais ring seat 16, concentric reducer 17, connecting tube 18, elbow 19 forms.Glais ring seat 16 both can rotate Glais ring 15 with installing hole, and the most also to 5 fixations of bearing, the adpting flange 1 near bearing end is connected with adpting flange 1 bolt of fin rotating drum by bearing air cover 2.
As preferably embodiment, described indirect steam outlet 6 is arranged on vaporization chamber top.
Work process:
Raw water delivers to multiple micro-spray painting day with fog by water pump, and micro-spray painting day with fog atomizes water into fine liquid particles group, and equal quality water surface area of drop after atomization is form liquid film surface area through tubulation filming device 200-1000 times, increases heat exchange area.Owing to the drop diameter after atomization is the least, the heat required for each water droplet phase transformation evaporation is few, substantially can accelerate evaporation rate with flash evapn, also can produce high-purity indirect steam simultaneously.Add vapours and entered rotating fins intracavity by heating vapour system through II type sound exchanger, under the effect of internals, form turbulent flow, carrying out heat exchange with fin, make fin temperature increase, a part of heat of fin outer wall is delivered to vaporization chamber by the convection action of steam, the water droplet group of motion is conducted heat, major part heat directly carries out heat exchange with the water droplet group impinging upon fin, makes drop phase transformation evaporate, and produces indirect steam.It is broken line mechanical periodicity that motor changes rotating speed under Frequency Converter Control, it is delivered under the effect of belt wheel on I type sound exchanger belt wheel, drive the rotation in fin chamber, play and promote the effect that heat exchange is uniform, increase thermal convection current, to increase the chaotic intensity of vaporization chamber air-flow, augmentation of heat transfer, destroys the motion structure of water droplet group, increases the heat transfer coefficient of water and fin outer wall.Aerofoil fan produces downward wind-force to the fluid domain between adjacent fins, adds drop in the movement time of vaporization chamber and air-flow confusion degree, further promotes water, effect that vapour separates simultaneously.
The above instrument is the preferred embodiment of the present invention, and protection scope of the present invention not instrument is confined to above-described embodiment, and 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 those skilled in the art, some improvements and modifications without departing from the principles of the present invention, these improvements and modifications also should be regarded as protection scope of the present invention.
Claims (8)
1. a spraying rotary steam generator, goes out including rotating fins chamber, vaporization chamber, I type sound exchanger, condensed water
Port system, II type sound exchanger and heating steam inlet system, it is characterised in that:
Described rotating fins chamber includes that fin is responsible for (21) and fin groove (11), and described fin supervisor (21) has porous,
Formation heat exchange main body it is connected with fin groove (11)；One end, described rotating fins chamber is connected with I type sound exchanger, the other end with
II type sound exchanger connects；
Described vaporization chamber includes evaporating locular wall (22), indirect steam outlet (6), first conduit (12) and spraying system
(23) outside, described vaporization chamber is set in rotating fins chamber and keep seal；
Described I type sound exchanger includes connecting tube (18) and belt pulley (13), and described belt pulley (13) is located at connecting tube
(18) outer wall；
Described condensation-water drain system includes the two ends that a concentric reducer (17), elbow (19) coordinate with concentric reducer (17)
The connecting tube (18) of different-diameter, adpting flange (1), described connecting tube (18) major diameter one end and adpting flange (1)
Connecting, described connecting tube (18) other end is connected with concentric reducer (17) one end, described concentric reducer (17) other end connecting bending
Head (19)；
Described II type sound exchanger includes the company of the two ends different-diameter that a concentric reducer (17) coordinates with concentric reducer (17)
Adapter (18), described connecting tube (18) minor diameter one end is connected with rotating fins chamber, connecting tube (18) major diameter one end and
Heating steam inlet system connects；
Described heating steam inlet system includes connecting tube (18) and the elbow (19) of relevant connection, described connecting tube (18)
It is connected with II type sound exchanger connecting tube (18) major diameter one end.
A kind of spraying rotary steam generator the most according to claim 1, it is characterised in that: described rotating fins chamber is also wrapped
Include adpting flange (1), jump ring (4), bearing (5), axle rotation Glais ring (8), aerofoil fan (10), size
Head (17) and connecting tube (18)；Described fin supervisor (21) is connected with connecting tube (18), then with concentric reducer (17) even
Connect, be then connected with adpting flange (1) by connecting tube (18).
Spraying rotary steam generator the most according to claim 2, it is characterised in that: described fin supervisor (21)
It is connected with the connecting tube (18) of radius ratio fin supervisor's (21) little 0.333 times of bearing inner race thickness.
A kind of spraying rotary steam generator the most according to claim 2, it is characterised in that: described vaporization chamber also includes
Include bearing air cover (2), bearing block (3), flange (7) and axle and rotate Glais ring groove (9)；Described bearing block (3) with
Flange (7) connects, and described bearing air cover (2) is connected with bearing block (3) single ended bolt, positions to bearing；Described flange (7)
Have Glais ring groove, axle rotation Glais ring (8) on rotating fins chamber is installed, vaporization chamber is sealed.
A kind of spraying rotary steam generator the most according to claim 2, it is characterised in that: described I type sound exchanger
Also include adpting flange (1), bearing air cover (2), jump ring (4), bearing (5), hole rotate Glais ring groove (15),
Glais ring seat (16) and concentric reducer (17)；Described belt pulley (13) is connected to connecting tube (18) outer wall；Near bearing end
(5) adpting flange (1) is connected with the adpting flange (1) of condensation-water drain system by bearing air cover (2), connection method
Washer sealing is had between blue (1).
A kind of spraying rotary steam generator the most according to claim 5, it is characterised in that: described II type sound exchanger
Also include that adpting flange (1), described connecting tube (18) minor diameter one end are connected with the adpting flange (1) in rotating fins chamber,
Connecting tube (18) major diameter one end is connected by the adpting flange (1) of bearing air cover (2) with heating steam inlet system.
A kind of spraying rotary steam generator the most according to claim 2, it is characterised in that: described heating steam inlet system
System also include 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)；Have hole on described Glais ring seat (16) and rotate Glais ring groove (15), with
Time to bearing (5) rise fixation；The adpting flange (1) held near bearing (5) is revolved with fin by bearing air cover (2)
The adpting flange (1) turning chamber connects.
Spraying rotary steam generator the most according to claim 1, it is characterised in that: described indirect steam outlet (6)
It is arranged on vaporization chamber top.
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 |
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| Publication Number | Publication Date |
|---|---|
| CN105910080A true CN105910080A (en) | 2016-08-31 |
| CN105910080B CN105910080B (en) | 2018-01-19 |
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ID=56745966
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610225227.5A Active CN105910080B (en) | 2016-04-13 | 2016-04-13 | One kind spraying rotary steam generator |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113648945A (en) * | 2021-08-13 | 2021-11-16 | 浙江工业大学 | Regulation and control method of device capable of achieving sufficient heating and temperature rise of micro-droplets |
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|---|---|---|---|---|
| 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 |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113648945A (en) * | 2021-08-13 | 2021-11-16 | 浙江工业大学 | Regulation and control method of device capable of achieving sufficient heating and temperature rise of micro-droplets |
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| Publication number | Publication date |
|---|---|
| CN105910080B (en) | 2018-01-19 |
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