Patent Grant
11815299
This application is based on and claims the benefit of priority from Chinese Patent Application No. 202110582960.3; filed on 27 May 2021, the entirety of which is incorporated by reference herein.
The present disclosure relates to the field of refrigerating technologies, and in particularly, to a refrigeration apparatus based on a molecular sieve.
A traditional refrigerating technology employs compressor compression to condense a refrigerant or employs a liquid to absorb the refrigerant, both of which have high energy consumption.
Several embodiments of the present disclosure provide a refrigeration apparatus based on a molecular sieve capable of refrigerating with lower power consumption.
A refrigeration apparatus based on a molecular sieve according to an embodiment of the present disclosure includes:
The refrigeration apparatus based on the molecular sieve according to the embodiment of the present disclosure at least has the following beneficial effects: an air flow alternately passes through the first molecular sieve device and the second molecular sieve device through the reversing valve, and then flows back through the balancing valve, so that the first molecular sieve device and the second molecular sieve device are regenerated. The first molecular sieve device and the second molecular sieve device are capable of separating a refrigerant from a depressurization gas, and the refrigerant is condensed after reaching a certain concentration to become a liquid refrigerant, and then enters an evaporator again for refrigeration. Energy consumption required in a condensing process of the refrigeration apparatus is lower, thus reducing a production cost of the refrigeration apparatus.
According to some embodiments of the present disclosure, the first blowing device includes a ventilator.
According to some embodiments of the present disclosure, the second blowing device includes a ventilator.
According to some embodiments of the present disclosure, the first air inlet interface is located at a top portion of the first storage tank.
According to some embodiments of the present disclosure, the first air outlet interface is located at an upper portion of the first storage tank and is located below the first air inlet interface.
According to some embodiments of the present disclosure, the liquid outlet is located at a bottom portion of the first storage tank.
According to some embodiments of the present disclosure, the refrigeration apparatus further includes a heat dissipating device, and the heat dissipating device is configured for dissipating heat for the first storage tank.
According to some embodiments of the present disclosure, the heat dissipating device includes a cooling container, at least a part of the first storage tank is located in the cooling container, and the cooling container is configured for placing cooling water to soak at least a part of the first storage tank.
According to some embodiments of the present disclosure, the fifth connecting pipe includes a liquid storage section, and the liquid storage section includes a plurality of U-shaped pipes.
According to some embodiments of the present disclosure, the first valve and/or the second valve are electronic valves.
Part of the additional aspects and advantages of the present disclosure will be given in part in the following description, and will become apparent in part from the following description, or will be learned through the practice of the present disclosure.
The present disclosure will be further explained with reference to the accompanying drawings and embodiments hereinafter, wherein:
101 refers to first connecting pipe; 102 refers to second connecting pipe; 103 refers to third connecting pipe; 104 refers to fourth connecting pipe; 105 refers to fifth connecting pipe; 106 refers to sixth connecting pipe; 107 refers to seventh connecting pipe; 108 refers to eighth connecting pipe; 109 refers to ninth connecting pipe; 110 refers to tenth connecting pipe; 111 refers to eleventh connecting pipe; 112 refers to twelfth connecting pipe; 113 refers to evaporator; 114 refers to first blowing device; 115 refers to first storage tank; 116 refers to second storage tank; 117 refers to second blowing device; 118 refers to first molecular sieve device; 119 refers to second molecular sieve device; 120 refers to reversing valve; 121 refers to first valve; 122 refers to second valve; 123 refers to balancing valve; 124 refers to first one-way valve; 125 refers to second one-way valve; and 126 refers to liquid storage section.
The embodiments of the present disclosure will be described in detail hereinafter. Examples of the embodiments are shown in the accompanying drawings. The same or similar reference numerals throughout the drawings denote the same or similar elements or elements having the same or similar functions. The embodiments described below with reference to the accompanying drawings are exemplary and are only intended to explain the present disclosure, but should not be construed as limiting the present disclosure.
In the description of the present disclosure, it shall be understood that the orientation or position relation related to the orientation description, such as the orientation or position relation indicated by the upper, lower, front, rear, left, right, etc., is based on the orientation or position relation shown in the drawings, which is only used for convenience of description of the present disclosure and simplification of description instead of indicating or implying that the indicated device or element must have a specific orientation, and be constructed and operated in a specific orientation, and thus shall not be understood as a limitation to the present disclosure.
In the description of the present disclosure, the meaning of several refers to be one or more, and the meaning of multiple refers to be more than two. The meanings of greater than, less than, more than, etc., are understood as not including this number, while the meanings of above, below, within, etc., are understood as including this number. If there is a description to the first and second, it is only for the purpose of distinguishing technical features, and shall not be understood as indicating or implying relative importance, implicitly indicating the number of the indicated technical features or implicitly indicating the order of the indicated technical features.
In the description of the present disclosure, unless otherwise clearly defined, words such as setting, installation, connection, etc., shall be understood broadly, and those skilled the art can reasonably determine the specific meanings of the above words in the present disclosure in combination with the specific contents of the technical solution.
With reference to
It shall be understood a refrigerant and a depressurization gas are injected into the refrigeration apparatus, and refrigerating cycle is implemented through cyclic conversion between a gaseous state and a liquid state of the refrigerant.
Specifically, the liquid refrigerant and the depressurization gas are mixed in the evaporator 113, and the evaporator 113 provides an evaporating space in a position where the liquid refrigerant and the depressurization gas start to be mixed. No gaseous refrigerant exists in the mixing position, which means that a partial pressure of the gaseous refrigerant is zero, so that the liquid refrigerant is inevitably evaporated to form the gaseous refrigerant. In this process, the evaporator 113 absorbs heat in air to implement refrigeration.
The gaseous refrigerant and the depressurization gas are mixed in the evaporator 113 to form a mixed gas, and the mixed gas enters the condensing assembly, with a flow direction controlled by the reversing valve 120, and then alternately passes through the first molecular sieve device 118 and the second molecular sieve device 119. The first molecular sieve device 118 and the second molecular sieve device 119 both include a molecular sieve. The molecular sieve has a function of sieving molecules, and is provided with a plurality of channels with a uniform aperture and orderly arranged holes in structure. The molecular sieves with different apertures separate molecules with different sizes and shapes. The first molecular sieve device 118 and the second molecular sieve device 119 are set to allow the depressurization gas to pass through and prevent the refrigerant from passing through, so as to separate the mixed gas.
For example, the refrigerant is selected to be ammonia, and the depressurization gas is selected to be hydrogen or helium. A molecular diameter of the hydrogen is 0.289 nm, which is namely 2.89 A. A molecular diameter of the helium is 0.26 nm, which is namely 2.6 A. A molecular diameter of the ammonia is 0.444 nm, which is namely 4.44 A. Therefore, the first molecular sieve device 118 and the second molecular sieve device 119 are selected to be 3 A or 4 A molecular sieves, both of which may effectively separate the hydrogen from the ammonia, or separate the helium from the ammonia.
The essence of liquefaction of the gaseous refrigerant is that when a relative humidity of the gaseous refrigerant reaches 100%, the gaseous refrigerant is inevitably liquefied. Therefore, after the mixed gas is separated, only the gaseous refrigerant remains in the condensing assembly, or the gaseous refrigerant and the liquid refrigerant exist at the same time. When the first blowing device 114 continuously leads the mixed gas into the first storage tank 115, the second blowing device 117 delivers the mixed gas to the first molecular sieve device 118 and the second molecular sieve device 119 to sieve the remaining refrigerant. After the relative humidity of the gaseous refrigerant reaches 100%, the gaseous refrigerant is condensed into the liquid refrigerant.
Microscopically, evaporation is a process of that liquid molecules leave from a liquid surface. Since the molecules in the liquid move constantly and irregularly, average kinetic energy of the molecules is compatible with a temperature of the liquid itself. Due to random movement and collision of the molecules, there are always some molecules with kinetic energy greater than the average kinetic energy at any moment. If these molecules with sufficient kinetic energy are close to the liquid surface, and the kinetic energy of these molecules is greater than power required to overcome an attractive force between the molecules in the liquid when the molecules fly out, these molecules can fly out from the liquid surface and become vapor of the liquid, which is the evaporation. After colliding with other molecules, the molecules flying out may return to the liquid surface or enter an interior of the liquid. If the molecules flying out are more than the molecules flying back, the liquid is evaporated. When there are more molecules in a space, the molecules flying back can be increased. When the molecules flying out are equal to the molecules flying back, the liquid is in a saturated state, and a pressure at the moment is called a saturation pressure Pt of the liquid at the temperature. At the moment, if a number of gaseous molecules of the substance in the space is artificially increased, a number of the molecules flying back may be greater than that of the molecules flying out, so that the condensation occurs.
The following describes a working process of the refrigeration apparatus with the ammonia as the refrigerant and the hydrogen as the depressurization gas.
Under the action of the second blowing device 117, the mixed gas of the ammonia and the hydrogen in the first storage tank 115 is pumped out and blown into the reversing valve 120. The reversing valve 120 controls an air flow to enter the first molecular sieve device 118 along the sixth connecting pipe 106, the first valve 121 is closed, the second valve 122 is opened, and a pressure at the sixth connecting pipe 106 is greater than that at the seventh connecting pipe 107. The mixed gas is filtered by the molecular sieve of the first molecular sieve device 118, the ammonia remains in the first molecular sieve device 118, the hydrogen mainly passes through the eighth connecting pipe 108 to the first one-way valve 124 and then enters the second storage tank 116, and a small part of the hydrogen flows into the balancing valve 123 from the eleventh connecting pipe 111. The hydrogen entering the second storage tank 116 flows out to the evaporator 113 along the tenth connecting pipe 110, the hydrogen flowing into the balancing valve 123 passes through the twelfth connecting pipe 112 and the ninth connecting pipe 109 and then enters the second molecular sieve device 119, and the residual ammonia in the molecular sieve device passes through the seventh connecting pipe 107 and the second valve 122 and then is pushed into the first storage tank 115, thus regenerating the molecular sieve of the second molecular sieve device 119.
With an increased concentration of the ammonia in the first storage tank 115, the ammonia is condensed into liquid ammonia and releases heat, and the liquid ammonia flows out through the fifth connecting pipe 105. In a process of entering the evaporator 113, a pressure is gradually decreased, and the liquid ammonia is vaporized and absorbs heat, which is mixed with the hydrogen flowing out from the tenth connecting pipe 110 in the evaporator 113. The mixed gas flows along the first connecting pipe 101 and continues to enter the first storage tank 115 along the second connecting pipe 102 with the help of the first blowing device 114, and then, under an action of the second blowing device 117, the mixed gas flows out from the third connecting pipe 103, thus completing one refrigerating cycle.
After a period of time, a direction is changed by the reversing valve 120, so that the mixed gas blown in by the second blowing device 117 flows to the second molecular sieve device 119, the first valve 121 is opened, the second valve 122 is closed, and a pressure at the sixth connecting pipe 106 is lower than that at the seventh connecting pipe 107. The mixed gas is filtered by the molecular sieve of the second molecular sieve device 119, the ammonia remains in the second molecular sieve device 119, the hydrogen mainly passes through the ninth connecting pipe 109 to the second one-way valve 125 and then enters the second storage tank 116, and a small part of the hydrogen flows into the balancing valve 123 from the twelfth connecting pipe 112. The hydrogen entering the second storage tank 116 flows out to the evaporator 113 along the tenth connecting pipe 110, the hydrogen flowing into the balancing valve 123 passes through the eleventh connecting pipe 111 and the eighth connecting pipe 108 and then enters the first molecular sieve device 118, and the residual ammonia in the molecular sieve device passes through the sixth connecting pipe 106 and the first valve 121 and then is pushed into the first storage tank 115, thus regenerating the molecular sieve of the second molecular sieve device 118.
An air flow alternately passes through the first molecular sieve device 118 and the second molecular sieve device 119 through the reversing valve 120, and then flows back through the balancing valve 123, so that the first molecular sieve device 118 and the second molecular sieve device 119 are regenerated. The first molecular sieve device 118 and the second molecular sieve device 119 are capable of separating a refrigerant from a depressurization gas, and the refrigerant is condensed after reaching a certain concentration to become a liquid refrigerant, and then enters the evaporator 113 again for refrigeration. Energy consumption required in a condensing process of the refrigeration apparatus is lower, thus reducing a production cost of the refrigeration apparatus.
According to some embodiments of the present disclosure, the first blowing device 114 includes a ventilator, and the second blowing device 117 includes a ventilator. The ventilator does not need a large compression ratio like a compressor of a conventional refrigeration apparatus, but only needs to lead the mixed gas into the first storage tank 115, and the condensation is implemented by a concentration change of the refrigerant itself. The ventilator generally has features of a low pressure difference and a large flow rate. Certainly, the first blowing device 114 and the second blowing device 117 may also be compressors, and power of the compressor may be smaller than that of a conventional compressor.
According to some embodiments of the present disclosure, the first air inlet interface is located at a top portion of the first storage tank 115. The first blowing device 114 supplements the mixed gas to the first storage tank 115, which is beneficial for protecting a pressure stability of a system and reducing an influence caused by one-side flowing of an air flow. A mass of the depressurization gas is less than that of the refrigerant, so that the depressurization gas may flow upwardly, and the refrigerant may go down. The first air inlet interface is located at the top portion of the first storage tank 115, which can reduce an influence on the concentration of the refrigerant at the lower portion of the first storage tank 115.
According to some embodiments of the present disclosure, the first air outlet interface is located at an upper portion of the first storage tank 115 and is located below the first air inlet interface. The first air outlet interface is close to the first air inlet interface, which can facilitate the second blowing device 117 to pump the mixed gas blown in by the first blowing device 114 into the reversing valve 120 to participate in the refrigerating cycle, so as to avoid pumping out the liquid ammonia at the bottom.
According to some embodiments of the present disclosure, the liquid outlet is located at a bottom portion of the first storage tank 115, which facilitates the liquefied refrigerant to flow out.
According to some embodiments of the present disclosure, the refrigeration apparatus further includes a heat dissipating device, and the heat dissipating device is configured for dissipating heat for the first storage tank 115. A heat dissipating efficiency of the first storage tank 115 can be effectively improved by arranging the heat dissipating device, and then a condensing efficiency of the condensing assembly is improved.
According to some embodiments of the present disclosure, the heat dissipating device includes a cooling container (not shown in the drawings), at least a part of the first storage tank 115 is located in the cooling container, and the cooling container is configured for placing cooling water to soak at least a part of the first storage tank 115, thus increasing a heat dissipating contact area. In order to improve a heat dissipating effect, a water inlet pipe and a water outlet pipe may be connected onto the cooling container to keep the cooling water in a certain stable range. Since a temperature difference of the first storage tank 115 is small, the cooling water pipe may use a normal temperature water source, which is convenient to take. It shall be understood the heat dissipating device may also adopt an air cooling device or a cooling water pipe, or the air cooling device may be used together with the cooling water pipe.
According to some embodiments of the present disclosure, the fifth connecting pipe 105 includes a liquid storage section 126, and the liquid storage section 126 includes a plurality of U-shaped pipes. More refrigerant can be stored and an occupied space of the fifth connecting pipe 105 is reduced by arranging the U-shaped pipes.
According to some embodiments of the present disclosure, the first valve 121 and/or the second valve 122 are electronic valves. Setting as the electronic valves is convenient for controlling automatically. It shall be understood the first valve 121 and the second valve 122 may also be set as mechanical valves.
The embodiments of the present disclosure are described in detail with reference to the drawings above, but the present disclosure is not limited to the above embodiments, and various changes may also be made within the knowledge scope of those of ordinary skills in the art without departing from the purpose of the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202110582960.3 | May 2021 | CN | national |
| Number | Name | Date | Kind |
|---|---|---|---|
| 20100242297 | Balerdi Azpilicueta | Sep 2010 | A1 |
| Number | Date | Country |
|---|---|---|
| 208694606 | Apr 2019 | CN |
| 110420536 | Nov 2019 | CN |
| Entry |
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| Yang (CN208694606U) English Translation, Efficient handling of unorganized emission VOCs's device, Apr. 5, 2019, Whole Document (Year: 2019). |
| Zhang (CN110420536A) English Translation, System and method for recovering VOCs at top of tank and reusing nitrogen gas, Aug. 11, 2019, Whole Document (Year: 2019). |
| Number | Date | Country | |
|---|---|---|---|
| 20220381490 A1 | Dec 2022 | US |
