CN203479029U - Condensation-proof smoke heat energy transferring device - Google Patents
Condensation-proof smoke heat energy transferring device Download PDFInfo
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- CN203479029U CN203479029U CN201320597655.2U CN201320597655U CN203479029U CN 203479029 U CN203479029 U CN 203479029U CN 201320597655 U CN201320597655 U CN 201320597655U CN 203479029 U CN203479029 U CN 203479029U
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Abstract
The utility model discloses a condensation-proof smoke heat energy transferring device and relates to the heat energy recycling technology. The condensation-proof smoke heat energy transferring device solves the problem of corrosion, caused by condensation, of a heat exchanger in the prior art. The condensation-proof smoke heat energy transferring device comprises a heat obtaining device. The heat obtaining device comprises a shell and a heat obtaining tube arranged in the shell. One end of the heat obtaining tube is communicated with an evaporator through a water outlet pipe. The evaporator is connected with the other end of the heat obtaining tube through a water inlet pipe. The condensation-proof smoke heat energy transferring device further comprises a heat exchanger. The heat exchanger is communicated with the evaporator through a steam pipe and a condensation pipe. An input pipeline and an output pipeline are arranged on the heat exchanger, wherein a lower-temperature medium is input through the input pipeline and a high-temperature medium is output through the output pipeline. A first temperature measurement instrument is arranged on the water inlet pipe. The fist temperature measurement instrument is connected with an automatic control system. The automatic control system can adjust the conveyance amount of the low-temperature medium input into the pipeline according to the temperature detected by the first temperature measurement instrument so that the temperature of liquid entering the evaporator and the water inlet pipe from the condensation pipe in sequence and finally reaching the heat obtaining pipe can be controlled to be higher than the smoke dew-point temperature in the heat obtaining device.
Description
Technical field
The utility model relates to heat energy recycle technology, relates in particular to a kind of not dewfall smoke heat energy and carries moving device.
Background technology
In modern industrial processes, there is a large amount of fume emissions, in the techniques such as sintering, cement kiln, glass furnace, coke oven, coal-burning boiler, gas fired-boiler, oil burning boiler, and contain amount of heat in the flue gas of discharge, be called fume afterheat, this fume afterheat resource belongs to secondary energy sources, is the product after primary energy or combustible material conversion, or the heat sending in fuel combustion process remaining heat after completing a certain technical process.
Particularly, in the flue gas of discharge, except containing amount of heat, conventionally also contain steam, oxygen sulfur compound, oxynitrides, dust etc., and flow is larger.If the discharge flue gas of Industrial Stoves, boiler etc. is not processed, directly enter in atmosphere, not only can cause environmental pollution, also can waste a large amount of heat energy in discharge flue gas, therefore, in order to respond country about energy-saving and cost-reducing, reduce the call of polluting, in prior art, a lot of enterprises, by coming the high-temperature region heat recovery and utilization in flue gas with equipment such as heat exchangers, are beneficial to environmental protection and the energy-saving and emission-reduction requirement now advocated.
Yet the surface temperature of entering fume side when heat exchanger is during lower than flue gas dew point, can there is dewfall phenomenon in its surface, be accompanied by flue gas and contain dust and oxygen sulfur compound, in dewfall, can cause the bonding of dust, thereby stop up flue, affects heat transfer effect; Also have acid simultaneously and reveal formation, cause the corrosion of heat exchanger, the danger such as heat exchanger leakage easily occur, have a strong impact on the service life of heat exchanger.
Utility model content
Embodiment of the present utility model provides a kind of not dewfall smoke heat energy to carry moving device, has solved the problem of heat exchanger dewing corrosion in prior art.
For achieving the above object, embodiment of the present utility model adopts following technical scheme:
A kind of not dewfall smoke heat energy carries moving device, comprise the heat collector that absorbs smoke heat energy, described heat collector comprises housing and is located at the heat removing tube in described housing, and described heat removing tube one end is communicated with evaporimeter by outlet pipe, and described evaporimeter is communicated with the described heat removing tube other end by water inlet pipe; Described not dewfall smoke heat energy carries moving device and also comprises thermal energy converter, and described thermal energy converter is communicated with described evaporimeter by steam pipe and condenser pipe respectively; Described thermal energy converter is provided with and passes into the input channel of cryogenic media, the output channel of output high-temperature medium; Described water inlet pipe is provided with the first temperature measurer, and described the first temperature measurer is connected with robot control system(RCS); The temperature that described robot control system(RCS) detects according to described the first temperature measurer, can regulate the conveying capacity of cryogenic media in described input channel, to control, from described condenser pipe, enter successively described evaporimeter, water inlet pipe, finally arrive the temperature of the liquid in described heat removing tube higher than the flue gas dew point in described heat collector.
Particularly, described evaporation tube is provided with the first adjuster, and described the first adjuster is connected with described robot control system(RCS); Described robot control system(RCS) is controlled described the first adjuster, regulates the evaporation capacity of described liquid in described evaporimeter.
Further, be also provided with filling pipe in described evaporimeter, described filling pipe is provided with the second adjuster, and described the second adjuster is connected with described robot control system(RCS); Described robot control system(RCS) is controlled described the second adjuster, to control described filling pipe, in described evaporimeter, fills into described liquid in good time, thereby regulates the liquid level of described liquid in described evaporimeter.
In order better automatically to control the first adjuster, described evaporimeter is provided with pressure detecting instrument, and described pressure detecting instrument is connected with described robot control system(RCS), and described robot control system(RCS) is controlled described the first adjuster automatically according to the detected value of described pressure detecting instrument.
In order better automatically to control the second adjuster, on described evaporimeter, be also provided with Level meter, described Level meter is connected with described robot control system(RCS), and described robot control system(RCS) is controlled described the second adjuster automatically according to the detected value of described Level meter.
Wherein, described liquid is desalted water; The temperature of described liquid is higher 5 degrees Celsius than described flue gas dew point temperature.
The structure of heat removing tube has multiple, is wherein a kind ofly: described heat removing tube comprises a plurality of longitudinal pipes that are parallel to each other, equidistantly arrange, and described longitudinal pipe two ends are equipped with the transverse pipe with described longitudinal pipe conducting; Described outlet pipe comprises two, is communicated with respectively with the described longitudinal pipe of both end sides; Described water inlet pipe is connected with the described transverse pipe that is positioned at lower end.
Preferably, along described heat removing tube bearing of trend, the ring fin that described heat removing tube outer surface is provided with and is a plurality ofly parallel to each other, equi-spaced apart arranges, the relative angle between described ring fin and described heat removing tube is adjustable; Described ring fin is fixed on described heat removing tube by nickel-based brazing, and the welding root between described ring fin and described heat removing tube surface is fillet.
Wherein, the fume side of entering of described heat collector is provided with flue gas flow guiding device or flue gas distributor; The heat removing tube of described heat collector is provided with the second temperature measurer, and described the second temperature measurer is for the surface temperature of heat removing tube described in Real-Time Monitoring.
Be specifically as follows, described flue gas flow guiding device comprises the arc track that a plurality of concentric circles arrange.
The not dewfall smoke heat energy that the utility model embodiment provides carries in moving device, comprise for absorbing the heat collector of discharge smoke heat energy, this heat collector comprises housing and is located at the heat removing tube in housing, by outlet pipe one end, be communicated with heat removing tube, the other end is communicated with evaporimeter, outlet pipe one end is communicated with heat removing tube, the other end is communicated with evaporimeter, complete the interconnection of heat collector and evaporimeter, be that liquid in heat removing tube arrives evaporimeter by outlet pipe, liquid in evaporimeter arrives in heat removing tube by water inlet pipe again, and evaporimeter is communicated with thermal energy converter by steam pipe and condenser pipe respectively, be that steam in evaporimeter enters thermal energy converter by steam pipe, the liquid obtaining after condensation in thermal energy converter is got back in evaporimeter by condenser pipe, in corresponding thermal energy converter, the input channel that passes into cryogenic media is set, the output channel of output high-temperature medium, thereby when in water inlet pipe, setting is connected with the first temperature measurer of robot control system(RCS), in the water inlet pipe that robot control system(RCS) can detect by the first temperature measurer, the temperature of liquid is adjusted the conveying capacity of cryogenic media in input channel, to control, from condenser pipe, enter successively evaporimeter, water inlet pipe, finally arrive fluid temperature in heat removing tube higher than the flue gas dew point in heat collector.Analyze thus known, the fluid temperature detecting when the first temperature measurer is during a little less than flue gas dew point, robot control system(RCS) can reduce the conveying capacity of cryogenic media, thereby indirectly improved the temperature that enters the liquid of evaporimeter from thermal energy converter by condenser pipe, thereby guaranteed from evaporimeter to arrive fluid temperature in heat removing tube higher than flue gas dew point by water inlet pipe, thereby guaranteed that heat removing tube surface dewfall phenomenon can not occur, therefore can not form acid dew and the parts such as corrosion heat collector yet, guaranteed the normal operation that dewfall smoke heat energy does not carry moving device, practicality is high.
Accompanying drawing explanation
Fig. 1 carries moving device structural representation for the not dewfall smoke heat energy that the utility model embodiment provides;
The heat removing tube structural representation that Fig. 2 provides for the utility model embodiment;
Fig. 3 is the partial schematic diagram amplifying in Fig. 2.
The specific embodiment
Below in conjunction with accompanying drawing to the utility model embodiment not dewfall smoke heat energy carry moving device and be described in detail.
The utility model embodiment provides a kind of not dewfall smoke heat energy to carry moving device, as shown in Figure 1, comprise the heat collector 10 that absorbs smoke heat energy, heat collector 10 comprises housing 101 and is located at the heat removing tube 102 in housing, heat removing tube 102 one end are communicated with evaporimeter 12 by outlet pipe 11, and evaporimeter 12 is communicated with heat removing tube 102 other ends by water inlet pipe 13; Dewfall smoke heat energy does not carry moving device and also comprises thermal energy converter 14, and thermal energy converter 14 is communicated with evaporimeter 12 by steam pipe 15 and condenser pipe 16 respectively; Thermal energy converter 14 is provided with and passes into the input channel 17 of cryogenic media, the output channel 18 of output high-temperature medium; Water inlet pipe 13 is provided with the first temperature measurer 20, the first temperature measurers 20 and is connected with robot control system(RCS) 21; The temperature that robot control system(RCS) 21 detects according to the first temperature measurer 20, can regulate the conveying capacity of cryogenic media in input channel 17, to control, from condenser pipe 16, enter successively evaporimeter 12, water inlet pipe 13, finally arrive the temperature of the liquid in heat removing tube 102 higher than the flue gas dew point in heat collector 10.
The not dewfall smoke heat energy that the utility model embodiment provides carries in moving device, comprise for absorbing the heat collector of discharge smoke heat energy, this heat collector comprises housing and is located at the heat removing tube in housing, by outlet pipe one end, be communicated with heat removing tube, the other end is communicated with evaporimeter, outlet pipe one end is communicated with heat removing tube, the other end is communicated with evaporimeter, complete the interconnection of heat collector and evaporimeter, be that liquid in heat removing tube arrives evaporimeter by outlet pipe, liquid in evaporimeter arrives in heat removing tube by water inlet pipe again, and evaporimeter is communicated with thermal energy converter by steam pipe and condenser pipe respectively, be that steam in evaporimeter enters thermal energy converter by steam pipe, the liquid obtaining after condensation in thermal energy converter is got back in evaporimeter by condenser pipe, in corresponding thermal energy converter, the input channel that passes into cryogenic media is set, the output channel of output high-temperature medium, thereby when in water inlet pipe, setting is connected with the first temperature measurer of robot control system(RCS), in the water inlet pipe that robot control system(RCS) can detect by the first temperature measurer, the temperature of liquid is adjusted the conveying capacity of cryogenic media in input channel, to control, from condenser pipe, enter successively evaporimeter, water inlet pipe, finally arrive fluid temperature in heat removing tube higher than the flue gas dew point in heat collector.Analyze thus known, the fluid temperature detecting when the first temperature measurer is during a little less than flue gas dew point, robot control system(RCS) can reduce the conveying capacity of cryogenic media, thereby indirectly improved the temperature that enters the liquid of evaporimeter from thermal energy converter by condenser pipe, thereby guaranteed from evaporimeter to arrive fluid temperature in heat removing tube higher than flue gas dew point by water inlet pipe, thereby guaranteed that heat removing tube surface dewfall phenomenon can not occur, therefore can not form acid dew and the parts such as corrosion heat collector yet, guaranteed the normal operation that dewfall smoke heat energy does not carry moving device, practicality is high.
It should be noted that herein, in Fig. 1, water inlet pipe 13 and outlet pipe 11 are liquid for the flow direction of heat removing tube 102, the mounting means that can certainly carry moving device according to dewfall smoke heat energy not defines, for example, because liquid self has constant weight, therefore conventionally dewfall smoke heat energy does not carry moving device and settles in vertical direction, now outlet pipe 11 also can be called tedge, and water inlet pipe 13 also can be called down-comer.
When practical application, fluid temperature in heat removing tube 102 remains on the numerical value higher than flue gas dew point, be specifically as follows by test and technical staff's experience, determine higher than 5 degrees Celsius of flue gas dew points (℃), certainly, also can be other reasonable numerical value, for example, in the deviation of 1 degree Celsius of 5 degrees Celsius of upper and lower existence, 5 ± 1 ℃.Now, the liquid entering in evaporimeter 12 by outlet pipe 11 from heat removing tube 102 is also higher than 5 degrees Celsius of flue gas dew points, and in evaporimeter, there is Evaporation Phenomenon, the state coexisting for water, vapour in evaporimeter 12, thereby the saturation temperature that need to guarantee the liquid in evaporimeter 12 maintains higher than 5 degrees Celsius of flue gas dew points, therefore, can complete by the evaporation capacity of controlling in evaporimeter 12.
Particularly, as shown in Figure 1, on the evaporation tube 15 that one end is communicated with evaporimeter 12, can be provided with the first adjuster 151, also can be called evaporation flow regulator, this first adjuster 151 is connected with robot control system(RCS) 21, thereby by robot control system(RCS) 21, control to adjust the first adjuster 151, thereby complete the control of the interior liquid evaporation amount of evaporimeter 12.Wherein, the first adjuster 151 can be a simple construction of switch, thus robot control system(RCS) 21 can control the opening degree of this construction of switch and complete control, can certainly be other electronic equipments etc.
In addition, when controlling the first adjuster 151 by robot control system(RCS) 21, it controls parameter can be the pressure in evaporimeter 12.Be specifically as follows, on evaporimeter 12 is interior, be provided with pressure detecting instrument 121, it can be the equipment such as pressure transmission device, thereby be connected with robot control system(RCS) 21 by pressure detecting instrument 121, the numerical value detecting is sent in robot control system(RCS) 21, robot control system(RCS) 21 can be controlled the first adjuster 151 according to this numerical value, for example, when pressure in the evaporimeter 12 that pressure detecting instrument 121 detects is larger (comparing with the pressure value presetting), feed back in robot control system(RCS) 21, and control the first adjuster 151 steam flow is increased; Pressure in the evaporimeter 12 that pressure detecting instrument 121 detects is hour (comparing with the pressure value presetting), contrary with above-mentioned control procedure.
When the steam in evaporimeter 12 enters into thermal energy converter 14 by steam pipe 15, by steam, to cryogenic media, heat, thereby output high-temperature medium completes the utilization of heat energy.Particularly, thermal energy converter 14 one end are provided with input channel 17, and cryogenic media enters thermal energy converter 14 from input channel 17, and flows in the flow duct in thermal energy converter 14, the last high-temperature medium afterwards of heating of exporting from output channel 18.Wherein, can on the outer wall of flow duct, along its bearing of trend, be wound around water back, this water back one end is connected with steam pipe 15, the other end is connected with condenser pipe 16, thereby steam flows in water back, and give the heating of the cryogenic media in flow duct, cryogenic media absorbs the heat of steam, makes steam-condensation become aqueous water, and finally from the water back other end, flow back into condenser pipe 16, and and then enter in evaporimeter 12.In this process, Condensation can be the condensation under saturated vapor, its temperature change is very little, and certainly under other states, the temperature of condensed liquid may reduce, lower than flue gas dew point, when it flows in evaporimeter 12 by condenser pipe 16, the whole temperature that reduces liquid in evaporimeter 12 of meeting, but because the content liquid in evaporimeter 12 is more, therefore in the short time, can not change, and can guarantee to flow into temperature in heat removing tube 102 higher than flue gas dew point by subsequent adjustment.
Wherein, the cryogenic media heating in thermal energy converter 14 can be aqueous water, can be also gas or other flowable material.In addition, in thermal energy converter 14, when heating, may produce excessive pressure and thermal energy converter 14 is caused to damage, also can as shown in Figure 1 outlet 19 be set in thermal energy converter, thus the pressure in time in balance thermal energy converter 14.
Yet, in the long-term process of using, owing to can being dissolved with oxygen in liquid, the noncondensing gaseous state such as hydrogen, the work of therefore carrying moving device at dewfall smoke heat energy is not done in process, this portion gas also can be taken away a part of steam and discharge, cause going out of liquid in evaporimeter 12, enter imbalance, therefore as shown in Figure 1, filling pipe 22 can be set in evaporimeter 12, this filling pipe 22 is provided with the second adjuster 221, and the second adjuster 221 is connected with robot control system(RCS) 21, thereby robot control system(RCS) 21 is by controlling the second adjuster 221, can control filling pipe 22 in good time to the interior feeding-in liquid of evaporimeter 12, to regulate the liquid level of evaporimeter 12 interior liquid.
Specifically in when application, can be by peephole and rule are set on evaporimeter 12, and the routine observation by technical staff completes moisturizing and operates, and also can on evaporimeter 12, Level meter be set, this Level meter is connected with robot control system(RCS).Level meter can detect in real time the liquid level of liquid in evaporimeter 12 and detected value is fed back in robot control system(RCS) 21, to facilitate record and to control as required the second adjuster 221, controls unlatching, closure and the opening degree etc. of filling pipe 22.
It should be noted that, flowing liquid in heat removing tube 102, evaporimeter 12 and each pipeline, can be desalted water herein, and desalted water has the not feature of burn into good effect of heat exchange, certainly, can be also other rational liquid.
The not dewfall smoke heat energy that above-described embodiment is described carries in moving device, on water inlet pipe 13, be provided with the first temperature measurer 20, these the first temperature measurer 20 Real-Time Monitorings enter the fluid temperature in the heat removing tube 102 of heat collector 10, when there is the accidents such as breakage for some reason in water inlet pipe 13, it enters fluid temperature in heat removing tube 102 may be lower than flue gas dew point, therefore the second temperature measurer 103 can be set on heat removing tube 102 surfaces, by the second temperature measurer 103, can detect the temperature of liquid in heat removing tube 102, thereby by the cooperation of the first temperature measurer 20 and the second temperature measurer 103, relatively etc., fully guarantee not occur dewfall phenomenon.Wherein, due to each pipeline, such as outlet pipe 11, water inlet pipe 13, steam pipe 15 etc. all has certain length, therefore liquid, within it in mobile process, can give out certain heat, and this part heat is less certainly, but in order fully to guarantee not dewfall, can by being set, the material of above-mentioned pipeline for example be designed to be incubated material, the loss of heat energy while preventing liquid flow.
In addition, the first temperature measurer 20 and the second temperature measurer 103 can only comprise temperature probe, connect the holding wire of temperature probe and robot control system(RCS) 21 and be arranged in the temperature indicator of robot control system(RCS) 21, thereby complete the monitoring of temperature, in addition, can also in the respective line arranging, design a humidostat, by robot control system(RCS) 21, control the adjusting that humidostat completes fluid temperature if desired, can be for directly liquid being carried out the heating of respective degrees or tube wall carried out to the heating of respective degrees, such as the generation of cataclysm of environment etc.
During practical operation, discharge flue gas random path when mobile of Industrial Stoves, boiler etc., i.e. the flue gas comparatively dense of certain area, the flue gas in another part region is more sparse, and this kind of phenomenon can affect the absorption of heat energy in 102 pairs of flue gases of heat removing tube.Therefore, can adopt as shown in fig. 1, the fume side of entering at heat collector 10 arranges flue gas flow guiding device 23, it comprises the arc track 231 that a plurality of concentric circles arrange, and preferably, between adjacent arc track 231, can contact, interval can, for zero, can certainly not be in contact with one another to be applicable to different occasions.These flue gas flow guiding device 23 one end are the fume side of entering towards heat collector 10 towards flue gas air inlet side, the other end, by this flue gas flow guiding device 23, can be by flue gas shunting, make to carry out mobile flue gas flow basic identical in each arc track, guarantee the uniformity in each orientation when flue gas enters heat collector 10, make the surperficial flue gas flow rate of each heat removing tube 102 substantially equal, the problem of flue gas bias current can not occur, thereby improve the heat-obtaining effect of heat removing tube 102.Certainly, also can use flue gas shunting device, can make equally flue gas uniform-flow through heat collector 10, determine the application scenario that concrete selection can be carried moving device according to dewfall smoke heat energy not.
Wherein, the structure of arc track 231, space are arranged also can carry out relative set according to the average discharge of flue gas, speed and uniformity, to reach flue gas object of Uniform Flow more in heat collector 10.
When the utilization of carrying out smoke heat energy by heat removing tube 102 is reclaimed, heat removing tube 102 can be a pipeline, also can adopt structure as shown in Figure 1, this heat removing tube 102 comprises a plurality of longitudinal pipes that are parallel to each other, equidistantly arrange, longitudinal pipe two ends are equipped with the transverse pipe with longitudinal pipe conducting, now outlet pipe 11 comprises two, be communicated with the longitudinal pipe of both end sides respectively, and water inlet pipe 13 is connected with the transverse pipe that is positioned at lower end, thereby by heat removing tube 102 is set to this kind of structure, can improve the heat transfer effect of flue gas and heat removing tube 102 interior liquid.
In addition, in order further to improve flue gas and heat removing tube 102 surface heat exchanging efficiency, can change the mode of direct contact, particularly, as shown in Figure 2, at the outer surface of each heat removing tube 102, along on its bearing of trend, be provided be a plurality ofly parallel to each other, ring fin 31 that equi-spaced apart arranges, the relative angle between this ring fin 31 and heat removing tube 102 is adjustable.In Fig. 2, the vertical setting in surface of ring fin 31 and heat removing tube 102, thereby first arrive on ring fin 31 by flue gas, ring fin 31 fully absorbs the heat energy of flue gas, be sent to again on heat removing tube 102, therefore can the angle of ring fin 31 and the heat transfer effect that the distance between structure and adjacent annular fin 31 fully improves flue gas and liquid be rationally set according to the composition of flue gas, flow direction etc.
Preferably, ring fin 31 can be fixed on heat removing tube 102 by nickel-based brazing, compare traditional high-frequency welding, it is fillet that the welding manner adopting in the present embodiment can make the welding root between ring fin 31 and heat removing tube 102 surfaces, rate of deposition reaches 100%, and the structure that root is fillet is difficult for dust stratification, can as shown in Figure 3, be specifically the partial schematic diagram of Fig. 2 amplification.
Thereby be the structure shown in Fig. 1 to Fig. 3 by global design heat collector 10, can improve its heat exchange area and heat exchange efficiency, conventionally the heat collector that uses the present embodiment to provide, after smoke gas flow process, the flue-gas temperature of its discharge end can be reduced to higher 10 to 15 degrees Celsius than flue gas dew point temperature, low 30 to 50 degrees Celsius compared to existing technology, heat recovery rate is high.And by the design of above-described embodiment, on the surface of heat removing tube 102, dewfall phenomenon can not occur, so it is bad that stifled ash, formation acid dew etc. can not occur, and reached energy-conservation object.
In description of the present utility model, it will be appreciated that, term " " center ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end ", " interior ", orientation or the position relationship of indications such as " outward " are based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, rather than device or the element of indication or hint indication must have specific orientation, with specific orientation structure and operation, therefore can not be interpreted as restriction of the present utility model.
Term " first ", " second " be only for describing object, and can not be interpreted as indication or hint relative importance or the implicit quantity that indicates indicated technical characterictic.Thus, one or more these features can be expressed or impliedly be comprised to the feature that is limited with " first ", " second ".In description of the present utility model, except as otherwise noted, the implication of " a plurality of " is two or more.
In description of the present utility model, it should be noted that, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, and for example, can be to be fixedly connected with, and can be also to removably connect, or connect integratedly; Can be mechanical connection, can be to be also electrically connected to; Can be to be directly connected, also can indirectly be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, can concrete condition understand the concrete meaning of above-mentioned term in the utility model.
In the description of this description, specific features, structure, material or feature can be with suitable mode combinations in any one or more embodiment or example.
The above; it is only the specific embodiment of the present utility model; but protection domain of the present utility model is not limited to this; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; can expect easily changing or replacing, within all should being encompassed in protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion by the described protection domain with claim.
Claims (10)
- One kind not dewfall smoke heat energy carry moving device, it is characterized in that, comprise the heat collector that absorbs smoke heat energy, described heat collector comprises housing and is located at the heat removing tube in described housing, described heat removing tube one end is communicated with evaporimeter by outlet pipe, and described evaporimeter is communicated with the described heat removing tube other end by water inlet pipe;Described not dewfall smoke heat energy carries moving device and also comprises thermal energy converter, and described thermal energy converter is communicated with described evaporimeter by steam pipe and condenser pipe respectively; Described thermal energy converter is provided with and passes into the input channel of cryogenic media, the output channel of output high-temperature medium;Described water inlet pipe is provided with the first temperature measurer, and described the first temperature measurer is connected with robot control system(RCS); The temperature that described robot control system(RCS) detects according to described the first temperature measurer, can regulate the conveying capacity of cryogenic media in described input channel, to control, from described condenser pipe, enter successively described evaporimeter, water inlet pipe, finally arrive the temperature of the liquid in described heat removing tube higher than the flue gas dew point in described heat collector.
- 2. not dewfall smoke heat energy according to claim 1 carries moving device, it is characterized in that, described evaporation tube is provided with the first adjuster, and described the first adjuster is connected with described robot control system(RCS);Described robot control system(RCS) is controlled described the first adjuster, regulates the evaporation capacity of described liquid in described evaporimeter.
- 3. not dewfall smoke heat energy according to claim 2 carries moving device, it is characterized in that, is also provided with filling pipe in described evaporimeter, and described filling pipe is provided with the second adjuster, and described the second adjuster is connected with described robot control system(RCS);Described robot control system(RCS) is controlled described the second adjuster, to control described filling pipe, in described evaporimeter, fills into described liquid in good time, thereby regulates the liquid level of described liquid in described evaporimeter.
- 4. not dewfall smoke heat energy according to claim 3 carries moving device, it is characterized in that, described evaporimeter is provided with pressure detecting instrument, and described pressure detecting instrument is connected with described robot control system(RCS), and described robot control system(RCS) is controlled described the first adjuster automatically according to the detected value of described pressure detecting instrument.
- 5. not dewfall smoke heat energy according to claim 3 carries moving device, it is characterized in that, on described evaporimeter, be also provided with Level meter, described Level meter is connected with described robot control system(RCS), and described robot control system(RCS) is controlled described the second adjuster automatically according to the detected value of described Level meter.
- 6. according to the not dewfall smoke heat energy described in claim 1-5 any one, carry moving device, it is characterized in that, described liquid is desalted water; The temperature of described liquid is higher 5 degrees Celsius than described flue gas dew point temperature.
- 7. not dewfall smoke heat energy according to claim 1 carries moving device, it is characterized in that, described heat removing tube comprises a plurality of longitudinal pipes that are parallel to each other, equidistantly arrange, and described longitudinal pipe two ends are equipped with the transverse pipe with described longitudinal pipe conducting; Described outlet pipe comprises two, is communicated with respectively with the described longitudinal pipe of both end sides; Described water inlet pipe is connected with the described transverse pipe that is positioned at lower end.
- 8. not dewfall smoke heat energy according to claim 7 carries moving device, it is characterized in that, along described heat removing tube bearing of trend, the ring fin that described heat removing tube outer surface is provided with and is a plurality ofly parallel to each other, equi-spaced apart arranges, the relative angle between described ring fin and described heat removing tube is adjustable;Described ring fin is fixed on described heat removing tube by nickel-based brazing, and the welding root between described ring fin and described heat removing tube surface is fillet.
- 9. not dewfall smoke heat energy according to claim 1 carries moving device, it is characterized in that, the fume side of entering of described heat collector is provided with flue gas flow guiding device or flue gas distributor;The heat removing tube of described heat collector is provided with the second temperature measurer, and described the second temperature measurer is for the surface temperature of heat removing tube described in Real-Time Monitoring.
- 10. not dewfall smoke heat energy according to claim 9 carries moving device, it is characterized in that, described flue gas flow guiding device comprises the arc track that a plurality of concentric circles arrange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201320597655.2U CN203479029U (en) | 2013-09-25 | 2013-09-25 | Condensation-proof smoke heat energy transferring device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320597655.2U CN203479029U (en) | 2013-09-25 | 2013-09-25 | Condensation-proof smoke heat energy transferring device |
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| CN203479029U true CN203479029U (en) | 2014-03-12 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103486869A (en) * | 2013-09-25 | 2014-01-01 | 杨君廷 | Dewing-free smoke heat energy carrying and transferring device |
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2013
- 2013-09-25 CN CN201320597655.2U patent/CN203479029U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103486869A (en) * | 2013-09-25 | 2014-01-01 | 杨君廷 | Dewing-free smoke heat energy carrying and transferring device |
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