CN215686851U - Heating assembly and heating device - Google Patents

Heating assembly and heating device Download PDF

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Publication number
CN215686851U
CN215686851U CN202122017968.3U CN202122017968U CN215686851U CN 215686851 U CN215686851 U CN 215686851U CN 202122017968 U CN202122017968 U CN 202122017968U CN 215686851 U CN215686851 U CN 215686851U
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inner container
liquid
heating
steam
water pump
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马向阳
罗金柳生
南春来
任浩南
徐尧
杨柳斌
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Guangdong Midea Consumer Electric Manufacturing Co Ltd
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Guangdong Midea Consumer Electric Manufacturing Co Ltd
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Abstract

The application provides a heating element and firing equipment belongs to life electrical apparatus technical field. The heating assembly includes: the inner container is provided with an accommodating cavity which is used for accommodating liquid; the water inlet end of the water pump is communicated with the accommodating cavity; the water inlet end of the heating device is communicated with the water outlet end of the water pump, and the heating device is used for heating liquid; one end of the turbulence device is communicated with the water outlet end of the heating device, and the other end of the turbulence device is communicated with the accommodating cavity. Wherein, after the liquid is heated into steam or a steam-liquid mixture, the steam enters the containing cavity through the flow disturbing device. Through the technical scheme of this application, promote the volatilization of chlorine in the running water, improve the dechlorination effect of water injection process.

Description

Heating assembly and heating device
Technical Field
The application belongs to the technical field of life electrical apparatus, particularly, relates to a heating element and a heating device.
Background
Water plays an important role in human life and is one of the most important material resources essential for human survival and development. Chlorine is added into water in order to prevent tap water from being polluted in the process of pipeline transmission. And due to residual chlorine, people rarely directly drink tap water, and generally boil the tap water for drinking. The existing chlorine removal technology reduces the content of chlorine in water by increasing the boiling time, and increases time consumption.
SUMMERY OF THE UTILITY MODEL
The embodiment aims at improving the technical problems that residual chlorine in water cannot be directly drunk and can be healthily drunk through heating treatment.
In view of the above, an object of the present application is to provide a heating assembly.
It is another object of the present application to provide a heating apparatus.
To achieve the above object, an embodiment according to a first aspect of the present application provides a heating assembly, including: the inner container is provided with an accommodating cavity which is used for accommodating liquid; the water inlet end of the water pump is communicated with the accommodating cavity; the water inlet end of the heating device is communicated with the water outlet end of the water pump, and the heating device is used for heating liquid; the vortex device, the one end of vortex device and heating device's play water end intercommunication, the other end of vortex device with hold the chamber intercommunication, wherein, after liquid heating becomes steam or vapour-liquid mixture, get into through the vortex device and hold the chamber.
According to an embodiment of a second aspect of the present application there is provided a heating apparatus comprising a housing: a heating assembly as in any one of the embodiments of the first aspect above, provided within the housing.
In an embodiment of the present application, the heating assembly includes an inner bladder, a water pump, a heating device, and a turbulator. The liquid is heated into steam or a steam-liquid mixture, and enters the containing cavity from the turbulence device, and after the steam enters the containing cavity of the inner container, the steam moves from bottom to top in the containing cavity in the form of bubbles, so that the turbulence effect is generated on the low-temperature liquid in the inner container, the volatilization of chlorine in the low-temperature liquid is promoted, and the time consumption for chlorine removal is reduced. Meanwhile, high-temperature steam enters the low-temperature liquid, the density of the high-temperature steam is far smaller than that of the liquid, and the temperature of the high-temperature steam is much higher than that of the liquid, so that the high-temperature steam can quickly exchange heat with the low-temperature liquid while moving quickly in the liquid, the heating speed of the liquid in the liner is increased, and the time consumption for dechlorination can be correspondingly reduced.
Additional aspects and advantages of embodiments in accordance with the present application will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of embodiments in accordance with the present application.
Drawings
FIG. 1 is a cross-sectional structural schematic of a heating assembly according to one embodiment of the present application;
FIG. 2 is a cross-sectional structural schematic of a heating assembly according to one embodiment of the present application;
FIG. 3 is a cross-sectional structural schematic of a heating assembly according to one embodiment of the present application;
FIG. 4 is an enlarged schematic view of the structure at A in FIG. 1;
fig. 5 is an enlarged schematic view of B in fig. 3.
Wherein, the correspondence between the reference numbers and the part names of fig. 1 to 5 is:
10: a heating assembly; 100: an inner container; 102: an isolation cover; 104: a water pump; 106: a controller; 108: a heating device; 110: a safety valve; 112: an exhaust valve; 114: a temperature sensor; 116: a semi-enclosed space; 118: a flow disturbing device; 120: a limiting part.
Detailed Description
In order that the above objects, features and advantages of embodiments according to the present application may be more clearly understood, embodiments according to the present application will be described in further detail below with reference to the accompanying drawings and detailed description. It should be noted that features of embodiments according to the present application may be combined with each other without conflict.
In the following description, numerous specific details are set forth to provide a thorough understanding of embodiments according to the present application, however, embodiments according to the present application may be practiced in other ways than those described herein, and therefore the scope of protection afforded by embodiments according to the present application is not limited by the specific embodiments disclosed below.
Some embodiments provided in accordance with the present application are described below with reference to fig. 1-5.
Example 1
As shown in fig. 1, an embodiment according to a first aspect of the present application provides a heating assembly 10 comprising a bladder 100, a water pump 104, a heating device 110, and a turbulator 118.
Specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity, and the water outlet end of the water pump 104 is communicated with the water inlet end of the heating device 110. The heating device 110 is used to heat the liquid flowing from the water pump 104. Both ends of the flow disturbing means 118 are in communication with the water outlet end of the heating means 110 and the receiving chamber, respectively. After the liquid is heated by the heating device 110 to form vapor or vapor-liquid mixture, the vapor or vapor-liquid mixture enters the accommodating cavity through the turbulence device 118, and turbulence is formed on the liquid in the accommodating cavity.
The heating assembly 10 according to the embodiment of the first aspect of the present application includes an inner container 100, a water pump 104, a heating device 110, and a spoiler 118. After the low-temperature liquid flows into the heating device 110 from the accommodating cavity of the inner container 100 through the water pump 104, the low-temperature liquid is heated in the heating device 110 to form high-temperature steam or a steam-liquid mixture. The vapor or vapor-liquid mixture enters the turbulator 118 and then enters the containment chamber. It can be understood that after the steam enters the accommodating cavity of the inner container 100, the steam moves in the accommodating cavity from bottom to top in the form of bubbles, and a turbulent flow effect is generated on the low-temperature liquid in the inner container 100, so that the volatilization of chlorine in the low-temperature liquid is promoted, and the time consumption for chlorine removal is reduced. Meanwhile, high-temperature steam enters the low-temperature liquid, the density of the high-temperature steam is far less than that of the liquid, and the temperature of the high-temperature steam is much higher than that of the liquid, so that the high-temperature steam can quickly exchange heat with the low-temperature liquid while moving in the liquid, the heating speed of the liquid in the liner 100 is increased, and accordingly the time consumption for dechlorination can be reduced.
More specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity. The water pump 104 can drive the liquid to flow, so as to accelerate the heat exchange speed, thereby increasing the temperature rise speed of the liquid in the liner 100. The water inlet end of the heating device 110 is in communication with the water outlet end of the water pump 104 to receive the water pump to deliver the entrained liquid. The heating device 110 only heats a small amount of liquid from the water pump 104, which is beneficial to quickly forming steam, improving the turbulent flow speed and accelerating the dechlorination speed. The turbulent flow device 118 utilizes the turbulent flow effect generated by the steam to promote the volatilization of the chlorine in the liquid, thereby improving the chlorine removal effect in the heating process. The inner container 100, the water pump 104, the heating device 110 and the turbulent flow device 118 are connected into a ring, and steam repeatedly enters the inner container to disturb flow, so that the dechlorination effect is enhanced.
Example 2
As shown in fig. 1, the embodiment according to the first aspect of the present application provides a heating assembly 10, which includes an inner container 100, a water pump 104, a heating device 110, and a flow disturbing device 118, where the number of the flow disturbing devices 118 may be one or more.
Specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity, and the water outlet end of the water pump 104 is communicated with the water inlet end of the heating device 110. The heating device 110 is used to heat the liquid flowing from the water pump 104. Both ends of the flow disturbing means 118 are in communication with the water outlet end of the heating means 110 and the receiving chamber, respectively. After the liquid is heated by the heating device 110 to form vapor or vapor-liquid mixture, the vapor or vapor-liquid mixture enters the accommodating cavity through the turbulence device 118, and turbulence is formed on the liquid in the accommodating cavity.
The heating assembly 10 according to the embodiment of the first aspect of the present application includes an inner container 100, a water pump 104, a heating device 110, and a spoiler 118. After the low-temperature liquid flows into the heating device 110 from the accommodating cavity of the inner container 100 through the water pump 104, the low-temperature liquid is heated in the heating device 110 to form high-temperature steam or a steam-liquid mixture. The vapor or vapor-liquid mixture enters the turbulator 118 and then enters the containment chamber. It can be understood that after the steam enters the accommodating cavity of the inner container 100, the steam moves in the accommodating cavity from bottom to top in the form of bubbles, and a turbulent flow effect is generated on the low-temperature liquid in the inner container 100, so that the volatilization of chlorine in the low-temperature liquid is promoted, and the time consumption for chlorine removal is reduced. Meanwhile, high-temperature steam enters the low-temperature liquid, the density of the high-temperature steam is far less than that of the liquid, and the temperature of the high-temperature steam is much higher than that of the liquid, so that the high-temperature steam can quickly exchange heat with the low-temperature liquid while moving in the liquid, the heating speed of the liquid in the liner 100 is increased, and accordingly the time consumption for dechlorination can be reduced.
More specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity. The water pump 104 can drive the liquid to flow, so as to accelerate the heat exchange speed, thereby increasing the temperature rise speed of the liquid in the liner 100. The water inlet end of the heating device 110 is in communication with the water outlet end of the water pump 104 to receive the water pump to deliver the entrained liquid. The heating device 110 only heats a small amount of liquid from the water pump 104, which is beneficial to quickly forming steam, improving the turbulent flow speed and accelerating the dechlorination speed. The turbulent flow device 118 utilizes the turbulent flow effect generated by the steam to promote the volatilization of the chlorine in the liquid, thereby improving the chlorine removal effect in the heating process. The inner container 100, the water pump 104, the heating device 110 and the turbulent flow device 118 are connected into a ring, and steam repeatedly enters the inner container to disturb flow, so that the dechlorination effect is enhanced.
The arrangement of the plurality of turbulence devices 118 can increase the turbulence quantity, enhance the turbulence effect, correspondingly improve the dechlorination efficiency and reduce the dechlorination time. It is understood that the cross-sectional area of turbulator 118 needs to be within a certain range of values. Specifically, the sum S of the cross-sectional areas of the plurality of turbulators 118 is 6mm or greater2And is less than or equal to 600mm2
In some embodiments, the sum of the cross-sectional areas of turbulators 118 is greater than or equal to 6mm2. Limiting the sum of the minimum cross-sectional areas of turbulators 118 is beneficial to avoid having too small a vapor bubble to lose the turbulating effect. While the sum of the cross-sectional areas of turbulators 118 is less than or equal to 600mm2. The sum of the maximum cross-sectional areas of the turbulent flow devices 118 is limited, which is beneficial to avoiding that the turbulent flow devices 118 are too large and are not easy to seal and install, and can also avoid safety accidents caused by too much steam entering the closed inner container 100 in a short time and too large pressure. In some embodiments, the sum S of the cross-sectional areas of the plurality of turbulators may be further defined as 42mm or greater2Is less than or equal to 168mm2. For example 42mm2、50mm2、80mm2、115mm2、128mm2、140mm2、153mm2、168mm2Any one of the above values. It will be appreciated that the cross-sectional area of a single turbulator may be 7mm2、10mm2、12mm2、15mm2、20mm2、28mm2Any one of the equivalent values.
Example 3
As shown in fig. 1, according to another embodiment of the first aspect of the present application, there is provided a heating assembly 10, which includes a tank 100, a preheating tank, a water pump 104, a heating device 110, and a flow disturbing device 118. The turbulator 118 is disposed on the preheat tank. The number of the spoiler 118 may be one or more.
Specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity, and the water outlet end of the water pump 104 is communicated with the water inlet end of the heating device 110. The heating device 110 is used to heat the liquid flowing from the water pump 104. The turbulator 118 is disposed on the preheating slot, which is in communication with the receiving cavity via the turbulator 118. The preheating tank is also communicated with the water outlet end of the heating device 110. After the liquid is heated by the heating device 110 to form steam or a steam-liquid mixture, the liquid firstly enters the preheating tank and then enters the accommodating cavity through the turbulence device 118 to form turbulence to the liquid in the accommodating cavity.
The heating assembly 10 according to the embodiment of the first aspect of the present application includes an inner container 100, a water pump 104, a heating device 110, and a spoiler 118. After the low-temperature liquid flows into the heating device 110 from the accommodating cavity of the inner container 100 through the water pump 104, the low-temperature liquid is heated in the heating device 110 to form high-temperature steam or a steam-liquid mixture. The vapor or vapor-liquid mixture enters the turbulator 118 and then enters the containment chamber. It can be understood that after the steam enters the accommodating cavity of the inner container 100, the steam moves in the accommodating cavity from bottom to top in the form of bubbles, and a turbulent flow effect is generated on the low-temperature liquid in the inner container 100, so that the volatilization of chlorine in the low-temperature liquid is promoted, and the time consumption for chlorine removal is reduced. Meanwhile, high-temperature steam enters the low-temperature liquid, the density of the high-temperature steam is far less than that of the liquid, and the temperature of the high-temperature steam is much higher than that of the liquid, so that the high-temperature steam can quickly exchange heat with the low-temperature liquid while moving in the liquid, the heating speed of the liquid in the liner 100 is increased, and accordingly the time consumption for dechlorination can be reduced.
More specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity. The water pump 104 can drive the liquid to flow, so as to accelerate the heat exchange speed, thereby increasing the temperature rise speed of the liquid in the liner 100. The water inlet end of the heating device 110 is in communication with the water outlet end of the water pump 104 to receive the water pump to deliver the entrained liquid. The heating device 110 only heats a small amount of liquid from the water pump 104, which is beneficial to quickly forming steam, improving the turbulent flow speed and accelerating the dechlorination speed. The turbulent flow device 118 utilizes the turbulent flow effect generated by the steam to promote the volatilization of the chlorine in the liquid, thereby improving the chlorine removal effect in the heating process. The inner container 100, the water pump 104, the heating device 110 and the turbulent flow device 118 are connected into a ring, and steam repeatedly enters the inner container to disturb flow, so that the dechlorination effect is enhanced.
The arrangement of the plurality of turbulence devices 118 can increase the turbulence quantity, enhance the turbulence effect, correspondingly improve the dechlorination efficiency and reduce the dechlorination time. It is understood that the cross-sectional area of turbulator 118 needs to be within a certain range of values. Specifically, the sum S of the cross-sectional areas of the plurality of turbulators 118 is 6mm or greater2And is less than or equal to 600mm2
In some embodiments, the sum of the cross-sectional areas of turbulators 118 is greater than or equal to 6mm2. Limiting the sum of the minimum cross-sectional areas of turbulators 118 is beneficial to avoid having too small a vapor bubble to lose the turbulating effect. Meanwhile, the sum of the cross sectional areas of the flow disturbing devices 118 is less than or equal to 600mm2. Limiting the sum of the maximum cross-sectional areas of turbulators 118 is advantageousThe situation that the turbulent flow device 118 is too large and is difficult to seal and install is avoided, and safety accidents caused by too much steam entering the sealed inner container 100 in a short time and too large pressure can also be avoided. In some embodiments, the sum S of the cross-sectional areas of the plurality of turbulators may be further defined as 42mm or greater2Is less than or equal to 168mm2. For example 42mm2、50mm2、80mm2、115mm2、128mm2、140mm2、153mm2、168mm2Any one of the above values. It will be appreciated that the cross-sectional area of a single turbulator may be 7mm2、10mm2、12mm2、15mm2、20mm2、28mm2Any one of the equivalent values.
Through the arrangement of the preheating groove, the steam or the steam-liquid mixture firstly enters the preheating groove, and heat exchange can be carried out between the steam or the steam-liquid mixture and adjacent liquid in the inner container 100 in the preheating groove, so that the liquid in the inner container 100 can be heated, the temperature of the liquid can be increased, and meanwhile, the temperature of the steam or the steam-liquid mixture can be reduced, and the temperature difference between the steam or the steam-liquid mixture and the liquid in the inner container 100 can be reduced. The steam after the temperature difference reduces gets into from vortex device 118 and holds the chamber after, is favorable to reducing the cavitation noise. It can be understood that the larger the temperature difference, the more easily bubbles formed by steam are broken, and the smaller the temperature difference, the less easily bubbles are broken accordingly, thereby reducing cavitation noise.
Example 4
According to yet another embodiment of the first aspect of the present application, there is provided a heating assembly 10 comprising a bladder 100, a preheating tank, a water pump 104, a heating device 110, and a flow perturbation device 118.
Specifically, the inner container 100 has a receiving cavity for receiving liquid. The bottom of the inner container 100 is provided with a preheating groove. The preheating tank is provided with a flow disturbing device 118. The number of the spoiler 118 may be one or more.
The water inlet end of the water pump 104 is communicated with the accommodating cavity, and the water outlet end of the water pump 104 is communicated with the water inlet end of the heating device 110. The heating device 110 is used to heat the liquid flowing from the water pump 104. The turbulator 118 is disposed on the preheating slot, which is in communication with the receiving cavity via the turbulator 118. The preheating tank is also communicated with the water outlet end of the heating device 110. After the liquid is heated by the heating device 110 to form steam or a steam-liquid mixture, the liquid firstly enters the preheating tank and then enters the accommodating cavity through the turbulence device 118 to form turbulence to the liquid in the accommodating cavity.
The heating assembly 10 according to the embodiment of the first aspect of the present application includes an inner container 100, a water pump 104, a heating device 110, and a spoiler 118. After the low-temperature liquid flows into the heating device 110 from the accommodating cavity of the inner container 100 through the water pump 104, the low-temperature liquid is heated in the heating device 110 to form high-temperature steam or a steam-liquid mixture. The vapor or vapor-liquid mixture enters the turbulator 118 and then enters the containment chamber. It can be understood that after the steam enters the accommodating cavity of the inner container 100, the steam moves in the accommodating cavity from bottom to top in the form of bubbles, and a turbulent flow effect is generated on the low-temperature liquid in the inner container 100, so that the volatilization of chlorine in the low-temperature liquid is promoted, and the time consumption for chlorine removal is reduced. Meanwhile, high-temperature steam enters the low-temperature liquid, the density of the high-temperature steam is far less than that of the liquid, and the temperature of the high-temperature steam is much higher than that of the liquid, so that the high-temperature steam can quickly exchange heat with the low-temperature liquid while moving in the liquid, the heating speed of the liquid in the liner 100 is increased, and accordingly the time consumption for dechlorination can be reduced.
More specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity. The water pump 104 can drive the liquid to flow, so as to accelerate the heat exchange speed, thereby increasing the temperature rise speed of the liquid in the liner 100. The water inlet end of the heating device 110 is in communication with the water outlet end of the water pump 104 to receive the water pump to deliver the entrained liquid. The heating device 110 only heats a small amount of liquid from the water pump 104, which is beneficial to quickly forming steam, improving the turbulent flow speed and accelerating the dechlorination speed. The turbulent flow device 118 utilizes the turbulent flow effect generated by the steam to promote the volatilization of the chlorine in the liquid, thereby improving the chlorine removal effect in the heating process. The inner container 100, the water pump 104, the heating device 110 and the turbulent flow device 118 are connected into a ring, and steam repeatedly enters the inner container to disturb flow, so that the dechlorination effect is enhanced.
The arrangement of the plurality of turbulence devices 118 can increase the turbulence quantity, enhance the turbulence effect, correspondingly improve the dechlorination efficiency and reduce the dechlorination time.It is understood that the cross-sectional area of turbulator 118 needs to be within a certain range of values. Specifically, the sum S of the cross-sectional areas of the plurality of turbulators 118 is 6mm or greater2And is less than or equal to 600mm2
In some embodiments, the sum of the cross-sectional areas of turbulators 118 is greater than or equal to 6mm2. Limiting the sum of the minimum cross-sectional areas of turbulators 118 is beneficial to avoid having too small a vapor bubble to lose the turbulating effect. Meanwhile, the sum of the cross sectional areas of the flow disturbing devices 118 is less than or equal to 600mm2. The sum of the maximum cross-sectional areas of the turbulent flow devices 118 is limited, which is beneficial to avoiding that the turbulent flow devices 118 are too large and are not easy to seal and install, and can also avoid safety accidents caused by too much steam entering the closed inner container 100 in a short time and too large pressure. In some embodiments, the sum S of the cross-sectional areas of the plurality of turbulators may be further defined as 42mm or greater2Is less than or equal to 168mm2. For example 42mm2、50mm2、80mm2、115mm2、128mm2、140mm2、153mm2、168mm2Any one of the above values. It will be appreciated that the cross-sectional area of a single turbulator may be 7mm2、10mm2、12mm2、15mm2、20mm2、28mm2Any one of the equivalent values.
Through the arrangement of the preheating groove, the steam or the steam-liquid mixture firstly enters the preheating groove, and heat exchange can be carried out between the steam or the steam-liquid mixture and adjacent liquid in the inner container 100 in the preheating groove, so that the liquid in the inner container 100 can be heated, the temperature of the liquid can be increased, and meanwhile, the temperature of the steam or the steam-liquid mixture can be reduced, and the temperature difference between the steam or the steam-liquid mixture and the liquid in the inner container 100 can be reduced. The steam after the temperature difference reduces gets into from vortex device 118 and holds the chamber after, is favorable to reducing the cavitation noise. It can be understood that the larger the temperature difference, the more easily bubbles formed by steam are broken, and the smaller the temperature difference, the less easily bubbles are broken accordingly, thereby reducing cavitation noise.
The preheating groove is arranged at the bottom of the inner container 100, and the heat exchange of steam or a steam-liquid mixture and liquid is facilitated to be accelerated by utilizing the principle that hot gas rises and cold gas falls, so that the heating efficiency is improved.
In some embodiments, the preheating groove may be formed by the bottom wall of the inner container 100, or may be formed by opening the bottom wall of the inner container 100, and a separate shielding cover 102 is additionally provided to form the preheating groove. Specifically, a part of the bottom wall of the inner container 100 is recessed into the accommodating chamber, and a preheating groove is formed at the recessed position. According to the structure, the preheating groove and the inner container are integrally formed, and the structure is stable. Turbulator 118 is a through hole disposed in a recessed location.
Alternatively, the bottom wall of the inner container 100 is opened and the insulation cover 102 with the flow perturbation device 118 is provided at the open position. The isolation cover 102 is detachably connected to the liner 100. So as to facilitate installation and maintenance.
As shown in fig. 1 and 4, further, at the opening position, the bottom wall of the inner container 100 is bent toward the bottom, or protrudes outward from the accommodating cavity. Meanwhile, a limiting part 120 is arranged at the opening, and the limiting part 120 is connected with the part, protruding out of the accommodating cavity, of the bottom wall. The isolation cover 102 is disposed on a side of the limiting portion 120 close to the accommodating cavity. By arranging the limiting part 120, the isolation cover 102 can be prevented from being separated from the inner container, so that the working stability and reliability of the isolation cover 102 are ensured.
The isolation cover 102 can temporarily separate the vapor from the liquid, so that the vapor can preheat the liquid and the temperature difference can be reduced.
Example 5
According to yet another embodiment of the first aspect of the present application, there is provided a heating assembly 10 comprising a bladder 100, a preheating tank, a water pump 104, a heating device 110, and a flow perturbation device 118.
Specifically, the inner container 100 has a receiving cavity for receiving liquid. A preheating groove is arranged on the side wall of the inner container 100. The preheating tank is provided with a flow disturbing device 118. The number of the spoiler 118 may be one or more.
The water inlet end of the water pump 104 is communicated with the accommodating cavity, and the water outlet end of the water pump 104 is communicated with the water inlet end of the heating device 110. The heating device 110 is used to heat the liquid flowing from the water pump 104. The turbulator 118 is disposed on the preheating slot, which is in communication with the receiving cavity via the turbulator 118. The preheating tank is also communicated with the water outlet end of the heating device 110. After the liquid is heated by the heating device 110 to form steam or a steam-liquid mixture, the liquid firstly enters the preheating tank and then enters the accommodating cavity through the turbulence device 118 to form turbulence to the liquid in the accommodating cavity.
The heating assembly 10 according to the embodiment of the first aspect of the present application includes an inner container 100, a water pump 104, a heating device 110, and a spoiler 118. After the low-temperature liquid flows into the heating device 110 from the accommodating cavity of the inner container 100 through the water pump 104, the low-temperature liquid is heated in the heating device 110 to form high-temperature steam or a steam-liquid mixture. The vapor or vapor-liquid mixture enters the turbulator 118 and then enters the containment chamber. It can be understood that after the steam enters the accommodating cavity of the inner container 100, the steam moves in the accommodating cavity from bottom to top in the form of bubbles, and a turbulent flow effect is generated on the low-temperature liquid in the inner container 100, so that the volatilization of chlorine in the low-temperature liquid is promoted, and the time consumption for chlorine removal is reduced. Meanwhile, high-temperature steam enters the low-temperature liquid, the density of the high-temperature steam is far less than that of the liquid, and the temperature of the high-temperature steam is much higher than that of the liquid, so that the high-temperature steam can quickly exchange heat with the low-temperature liquid while moving in the liquid, the heating speed of the liquid in the liner 100 is increased, and accordingly the time consumption for dechlorination can be reduced.
More specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity. The water pump 104 can drive the liquid to flow, so as to accelerate the heat exchange speed, thereby increasing the temperature rise speed of the liquid in the liner 100. The water inlet end of the heating device 110 is in communication with the water outlet end of the water pump 104 to receive the water pump to deliver the entrained liquid. The heating device 110 only heats a small amount of liquid from the water pump 104, which is beneficial to quickly forming steam, improving the turbulent flow speed and accelerating the dechlorination speed. The turbulent flow device 118 utilizes the turbulent flow effect generated by the steam to promote the volatilization of the chlorine in the liquid, thereby improving the chlorine removal effect in the heating process. The inner container 100, the water pump 104, the heating device 110 and the turbulent flow device 118 are connected into a ring, and steam repeatedly enters the inner container to disturb flow, so that the dechlorination effect is enhanced.
The arrangement of the plurality of turbulence devices 118 can increase the turbulence quantity, enhance the turbulence effect, correspondingly improve the dechlorination efficiency and reduce the dechlorinationChlorine time. It is understood that the cross-sectional area of turbulator 118 needs to be within a certain range of values. Specifically, the sum S of the cross-sectional areas of the plurality of turbulators 118 is 6mm or greater2And is less than or equal to 600mm2
In some embodiments, the sum of the cross-sectional areas of turbulators 118 is greater than or equal to 6mm2. Limiting the sum of the minimum cross-sectional areas of turbulators 118 is beneficial to avoid having too small a vapor bubble to lose the turbulating effect. Meanwhile, the sum of the cross sectional areas of the flow disturbing devices 118 is less than or equal to 600mm2. The sum of the maximum cross-sectional areas of the turbulent flow devices 118 is limited, which is beneficial to avoiding that the turbulent flow devices 118 are too large and are not easy to seal and install, and can also avoid safety accidents caused by too much steam entering the closed inner container 100 in a short time and too large pressure. In some embodiments, the sum S of the cross-sectional areas of the plurality of turbulators may be further defined as 42mm or greater2Is less than or equal to 168mm2. For example 42mm2、50mm2、80mm2、115mm2、128mm2、140mm2、153mm2、168mm2Any one of the above values. It will be appreciated that the cross-sectional area of a single turbulator may be 7mm2、10mm2、12mm2、15mm2、20mm2、28mm2Any one of the equivalent values.
Through the arrangement of the preheating groove, the steam or the steam-liquid mixture firstly enters the preheating groove, and heat exchange can be carried out between the steam or the steam-liquid mixture and adjacent liquid in the inner container 100 in the preheating groove, so that the liquid in the inner container 100 can be heated, the temperature of the liquid can be increased, and meanwhile, the temperature of the steam or the steam-liquid mixture can be reduced, and the temperature difference between the steam or the steam-liquid mixture and the liquid in the inner container 100 can be reduced. The steam after the temperature difference reduces gets into from vortex device 118 and holds the chamber after, is favorable to reducing the cavitation noise. It can be understood that the larger the temperature difference, the more easily bubbles formed by steam are broken, and the smaller the temperature difference, the less easily bubbles are broken accordingly, thereby reducing cavitation noise.
As shown in fig. 3 and 5, the preheating groove is disposed on the side wall of the inner container 100, and the water pressure is relatively low, which is beneficial to reducing the working pressure of the water pump and improving the air intake efficiency. In addition, the preheating groove is arranged on the side wall of the inner container 100, so that the installation and maintenance are convenient.
In some embodiments, the preheating groove may be formed by a sidewall of the inner container 100. Specifically, a part of the side wall of the inner container 100 is recessed into the accommodating chamber, and a preheating groove is formed at the recessed position. According to the structure, the preheating groove and the inner container are integrally formed, and the structure is stable. Turbulator 118 is a through hole disposed in a recessed location.
The heating assembly 10 further includes an exhaust valve 112, the exhaust valve 112 being in communication with the preheating tank and enclosing a semi-enclosed space 116.
Alternatively, the inner bladder 100 is open on its side wall and the isolation cover 102 with the turbulators 118 is placed in the open position. The isolation cover 102 is detachably connected to the liner 100. So as to facilitate installation and maintenance.
Example 6
As shown in fig. 1, according to yet another embodiment of the first aspect of the present application, there is provided a heating assembly 10 including a bladder 100, a preheating tank, a water pump 104, a heating device 110, an exhaust valve 112, and a turbulator 118. The turbulator 118 is disposed on the preheat tank. The number of the spoiler 118 may be one or more.
Specifically, the inner container 100 has a receiving cavity for receiving liquid. The water inlet end of the water pump 104 is communicated with the accommodating cavity, and the water outlet end of the water pump 104 is communicated with the water inlet end of the heating device 110. The heating device 110 is used to heat the liquid flowing from the water pump 104. The turbulator 118 is disposed on the preheating slot, which is in communication with the receiving cavity via the turbulator 118. The preheating tank is also communicated with the water outlet end of the heating device 110. After the liquid is heated by the heating device 110 to form steam or a steam-liquid mixture, the liquid firstly enters the preheating tank and then enters the accommodating cavity through the turbulence device 118 to form turbulence to the liquid in the accommodating cavity.
The exhaust valve 112 is disposed at the notch position of the preheating bath. The preheat bath and vent valve 112 enclose a semi-enclosed space 116. Vent valve 112 is opened and steam enters semi-enclosed space 116. The exhaust valve 112 is closed, and the steam cannot enter the semi-closed space, and cannot enter the accommodating cavity. By the arrangement of the exhaust valve 112, whether the steam enters the accommodating chamber or not can be freely controlled. In addition, by adjusting the opening of the exhaust valve 112, the amount of steam entering the accommodating chamber can also be controlled.
It will be appreciated that the volume of the semi-enclosed space 116 cannot be too large to avoid reducing the effectiveness of removing cavitation noise. The semi-enclosed space 116 cannot be too small to avoid too small an amount of steam that would reduce the chlorine removal effect. In some embodiments, the volume V of the semi-enclosed space 116 and the bladder volume V0The ratio of the two is greater than or equal to 0.001 and less than or equal to 0.05. I.e. 0.001. ltoreq. V/V0Less than or equal to 0.05. Further, V/V0Greater than or equal to 0.0025 and less than or equal to 0.01. For example, V/V0The average particle diameter is any of 0.0025, 0.0028, 0.0035, 0.0048, 0.0056, 0.0067, 0.0072, 0.008, 0.0091, 0.0099, 0.01, and the like.
In some embodiments, the volume of the semi-enclosed space 116 is set to 2cm3To 100cm3In the meantime. For example 2cm3、5cm3、15cm3、30cm3、35cm3、40cm3、60cm3、75cm3、80cm3、90cm3、100cm3Any one of the above values.
The volume of the semi-enclosed space 116 may be further limited to 5cm3To 20cm3E.g. 2cm3、6cm3、8cm3、10cm3、20cm3Any one of the above values.
Example 7
On the basis of any one of the above embodiments, the water inlet end of the water pump 104 is arranged at the bottom of the inner container 100.
The water inlet end of the water pump 104 is arranged at the bottom of the inner container 100, so that the water pressure at the bottom can be utilized, the difficulty of pumping water by the water pump 104 is reduced, energy is saved, and consumption is reduced. In addition, generally speaking, the liquid with lower temperature is located at the bottom, and therefore, by arranging the water inlet end of the water pump 104 at the bottom of the inner container 100, the liquid with lower temperature in the accommodating cavity is favorably pumped into the heating device 108 for heating, so that the heating speed of the liquid in the entire accommodating cavity is increased.
In other embodiments, the water inlet end of the water pump 104 is not limited to be disposed at the bottom of the inner container 100, but may be disposed on the sidewall of the inner container 100. In this way, the processing and sealing arrangement of the inner container 100 is facilitated. The water inlet end is properly higher than the bottom of the inner container 100, which is also beneficial to avoiding water leakage during assembly and disassembly.
As shown in fig. 2, it can be understood that the distance H from the water inlet end of the water pump 104 to the bottom of the liner 100 is limited to a certain range. Due to the different sizes of the inner container 100, the total height H of the side wall of the inner container is determined by limiting the distance H from the water inlet end of the water pump 104 to the bottom of the inner container 1000The ratio between the two limits the size of H. In particular, the ratio H/H is defined0Greater than zero and less than or equal to 0.26. For example the ratio H/H0Is any one of values of 0.05, 0.06, 0.07, 0.079, 0.088, 0.1, 0.12, 0.15, 0.158, 0.18, 0.20 and 0.26.
In a further embodiment, the ratio H/H is defined0Greater than 0.079 and less than or equal to 0.158.
The distance H from the water inlet end of the water pump 104 to the bottom of the inner container 100 and the total height H of the side wall of the inner container 100 are limited0The ratio range therebetween is favorable for avoiding that the water inlet end of the water pump 104 is higher than the liquid level in the accommodating cavity and cannot pump water due to the overlarge distance H.
In some embodiments, the distance from the water inlet end of the water pump 104 to the bottom of the liner 100 can be further limited to 15mm to 30 mm. For example, the distance is any one of 15mm, 18mm, 20mm, 22mm, 25mm, and 30 mm.
In any of the above embodiments, the heating assembly 10 further includes a controller 106, a temperature sensor 114. The temperature sensor 114 is used to detect the temperature of the liquid in the accommodating chamber of the inner container 100. The temperature sensor 114 is electrically connected to the controller 106, and the controller 106 is electrically connected to the water pump 104 and the heating device 108. The temperature sensor 114 is arranged to detect the liquid temperature, so that the controller 106 can flexibly control the operation of the heating device 108 and the water pump 104 according to the liquid temperature, thereby improving the working efficiency or reducing the energy consumption. For example, when the temperature sensor 114 detects that the liquid temperature is above 98 ℃, or detects that the liquid temperature has not changed for a certain period of time, for example, 30 seconds, it is determined that the liquid in the inner container has boiled, and there is no need to continue heating. The operation of the heating device 108 and the water pump 104 may be stopped at this time to avoid wasting energy. Of course, the threshold for the duration judgment that the liquid temperature is kept constant may be 30 seconds, and may also be other time periods, such as 40 seconds, 1 minute, 20 seconds, and so on.
The temperature sensor 114 may be disposed at the bottom of the inner container 100, or may be disposed on a side wall of the inner container 100.
In any of the above embodiments, the heating assembly 10 further comprises a safety valve 110. A relief valve 110 is provided on the heating device 108. When the pressure at the heating device 108 is high, the safety valve 110 can be opened to release the pressure, so that the safety of the operation of the heating device 108 can be improved.
Example 8
According to an embodiment of a second aspect of the present application, there is provided a heating apparatus comprising a housing and a heating assembly 10 as described above in any one of the embodiments of the first aspect. The heating assembly 10 is disposed within the housing.
In this embodiment, the heating apparatus includes the heating assembly 10 of the above embodiment, so as to have all the beneficial effects of the above embodiment, which will not be described herein again. The housing is configured to provide protection to the heating assembly 10 therein from external interference.
Example 9
The heating assembly 10 according to one embodiment of the present application includes a bladder 100, a semi-enclosed space 116, a turbulator 118, a shield 102, a water pump 104, a controller 106, a heating device 108, a relief valve 110, a vent valve 112, and a temperature sensor 114.
Specifically, the inner container 100 contains a liquid. Taking tap water as an example, the water inlet end of the water pump 104 is connected with the inner container 100. The water outlet end of the water pump 104 is connected to a heating device 108. The heating device 108 heats the low-temperature water into steam or a mixture of hot water and steam, and then the steam enters the inner container 100. The steam or the mixture of the hot water and the steam heats the low-temperature water in the inner container 100 and generates a turbulent flow effect. The exhaust valve 112 is connected with the bottom or the side wall of the inner container 100, and the steam in the exhaust valve 112 does not directly enter the inner container 100, but enters a semi-closed space 116 first, and then enters the inner container 100 through a turbulent flow device 118 communicated with the semi-closed space 116, so that the water in the inner container 100 is heated while a turbulent flow effect is generated, and the volatilization of chlorine in the tap water is promoted.
Specifically, the semi-enclosed space 116 may be defined by the bottom/side wall of the inner container 100 and the exhaust valve 112, or may be defined by the inner container 100, the isolation cover 102 and the exhaust valve 112. In any case, the semi-enclosed space 116 is in communication with the housing of the bladder 100 by the flow perturbation means 118. The purpose of this design is: steam temperature is higher, directly gets into inner bag 100, and is great with liquid temperature difference in the inner bag 100, can produce great cavitation noise, nevertheless gets into semi-enclosed space 116 earlier, can improve the temperature of water to the water heating in this space fast, reduces with the difference in temperature of steam to greatly reduced cavitation noise, and this enclosed space can play certain isolation effect to the noise.
The heating device 108 is connected with a safety valve 110 besides an inlet/outlet channel, and can exhaust and release pressure to play a role in protection when the pressure in the pipeline is too high under abnormal conditions.
The bottom of the inner container 100 is provided with a temperature sensor 114, and when the water temperature is detected to be more than 98 ℃ or not changed for more than 30 seconds, the water is considered to be boiled, and a temperature signal is transmitted to the controller 106 so as to stop heating.
It can be understood that the hot steam generated by the heating device 108 heats the tap water, and the turbulent flow effect generated by the steam promotes the volatilization of chlorine in the tap water while the heating effect is achieved, so that the chlorine removal effect in the water boiling process is improved. The semi-enclosed space 116 cannot be too large in volume to have the effect of reducing cavitation noise.
In this embodiment, the connection position of the water pump 104 and the inner container 100 may be a bottom or a side wall, but when the water pump 104 is connected to the side wall, the distance between the water inlet end of the water pump 104 and the bottom of the inner container 100 is defined as 0 < H < 50mm, preferably 15mm < H < 30 mm.
The exhaust valve 112 and the liner 100 enclose a semi-closed space 116, or the exhaust valve 112, the isolation cover 102 and the liner 100 enclose a semi-closed space 116, and the semi-closed space 116 may be at the bottom of the liner 100 or at the side wall. The volume of the semi-enclosed space 116 is defined as 2cm 3. ltoreq. V.ltoreq.100 cm3, preferably 5cm 3. ltoreq. V.ltoreq.20 cm 3.
When the exhaust valve, the isolation cover and the inner container enclose a semi-closed space, the isolation cover is provided with a plurality of through holes as turbulence devices. The area of a single through-hole, or cross-sectional area of a single spoiler, is limited to 3mm2≤S≤75mm2Preferably 7mm2≤S≤28mm2Allowing water and steam to pass through. The isolation cover and the inner container can be fixedly connected or detachably connected.
In embodiments according to the present application, the terms "first", "second", "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance; the term "plurality" means two or more unless expressly limited otherwise. The terms "mounted," "connected," "fixed," and the like are to be construed broadly, and for example, "connected" may be a fixed connection, a removable connection, or an integral connection; "coupled" may be direct or indirect through an intermediary. Specific meanings of the above terms in the embodiments according to the present application can be understood by those of ordinary skill in the art as the case may be.
In the description of the embodiments according to the present application, it should be understood that the terms "upper", "lower", "left", "right", "front", "rear", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, only for convenience of description and simplification of description of the embodiments according to the present application, and do not indicate or imply that the referred devices or units must have a specific direction, be configured and operated in a specific orientation, and thus, cannot be construed as limitations on the embodiments according to the present application.
In the description herein, the description of the terms "one embodiment," "some embodiments," "specific embodiments," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example in accordance with the application. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The above embodiments are merely preferred embodiments according to the present application, and are not intended to limit the embodiments according to the present application, and those skilled in the art may make various modifications and variations to the embodiments according to the present application. Any modification, equivalent replacement, improvement and the like made within the spirit and principle of the embodiments according to the present application shall be included in the protection scope of the embodiments according to the present application.

Claims (15)

1. A heating assembly, comprising:
the inner container is provided with an accommodating cavity, and the accommodating cavity is used for accommodating liquid;
the water inlet end of the water pump is communicated with the accommodating cavity;
the water inlet end of the heating device is communicated with the water outlet end of the water pump, and the heating device is used for heating liquid;
one end of the turbulence device is communicated with the water outlet end of the heating device, the other end of the turbulence device is communicated with the accommodating cavity,
wherein, after the liquid is heated into steam or a steam-liquid mixture, the steam or the steam-liquid mixture enters the accommodating cavity through the flow disturbing device.
2. The heating assembly of claim 1,
the number of the flow disturbing devices is multiple;
the sum of the cross sectional areas of the turbulent flow devices is more than or equal to 6mm2And is less than or equal to 600mm2
3. The heating assembly of claim 1 or 2, further comprising:
the preheating groove is arranged in the inner container, the turbulent flow device is arranged on the preheating groove, and the water outlet end of the heating device is communicated with the turbulent flow device through the preheating groove.
4. The heating assembly of claim 3,
the preheating groove is arranged at the bottom of the inner container, or
Is arranged on the side wall of the inner container.
5. The heating assembly of claim 4,
a part of the bottom wall of the inner container is sunken towards the accommodating cavity to form the preheating groove; or
And part of the side wall of the inner container is sunken towards the accommodating cavity to form the preheating groove.
6. The heating assembly of claim 4,
an opening is formed in the bottom wall or the side wall of the inner container;
the heating assembly further comprises:
the isolation cover is arranged at the opening, the turbulence device is arranged on the isolation cover, and the isolation cover and the inner container construct the preheating groove.
7. The heating assembly of claim 6,
at the opening position, part of the bottom wall of the inner container protrudes out of the accommodating cavity;
the opening is also provided with a limiting part connected with the bottom wall, and the limiting part is used for limiting the isolation cover to be separated from the inner container.
8. The heating assembly of claim 3, further comprising:
and the exhaust valve is arranged at the notch position of the preheating groove and surrounds the preheating groove to form a semi-closed space, one end of the exhaust valve is communicated with the semi-closed space, and the other end of the exhaust valve is communicated with the water outlet end of the heating device.
9. The heating assembly of claim 8,
the ratio of the volume of the semi-closed space to the volume of the inner container is more than or equal to 0.001 and less than or equal to 0.05.
10. Heating assembly according to claim 1 or 2,
the water inlet end of the water pump is connected to the bottom of the inner container.
11. Heating assembly according to claim 1 or 2,
the water inlet end of the water pump is connected to the side wall of the inner container;
the ratio of the distance between the water inlet end of the water pump and the bottom of the inner container to the total height of the side wall is larger than zero and is less than or equal to 0.26.
12. The heating assembly of claim 1 or 2, further comprising:
and the controller is electrically connected with the water pump and the heating device respectively and is used for controlling the operation of the water pump and the heating device.
13. The heating assembly of claim 12, further comprising:
the temperature sensor is arranged on the inner container and electrically connected with the controller, the temperature sensor is used for detecting the temperature of liquid in the inner container, and the controller is further used for controlling the operation of the water pump and the heating device according to the temperature of the liquid.
14. The heating assembly of claim 1 or 2, further comprising:
the safety valve is arranged on the heating device and used for releasing pressure.
15. A heating apparatus, comprising:
a housing;
a heating assembly as claimed in any one of claims 1 to 14, provided within the housing.
CN202122017968.3U 2021-08-25 2021-08-25 Heating assembly and heating device Active CN215686851U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202122017968.3U CN215686851U (en) 2021-08-25 2021-08-25 Heating assembly and heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202122017968.3U CN215686851U (en) 2021-08-25 2021-08-25 Heating assembly and heating device

Publications (1)

Publication Number Publication Date
CN215686851U true CN215686851U (en) 2022-02-01

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
CN (1) CN215686851U (en)

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