CN109764516B

CN109764516B - Energy system, control method thereof and storage medium

Info

Publication number: CN109764516B
Application number: CN201910019234.3A
Authority: CN
Inventors: 于洋
Original assignee: Qingdao Haier Air Conditioner Gen Corp Ltd; Haier Smart Home Co Ltd; Chongqing Haier Air Conditioner Co Ltd
Current assignee: Qingdao Haier Air Conditioner Gen Corp Ltd; Haier Smart Home Co Ltd; Chongqing Haier Air Conditioner Co Ltd
Priority date: 2019-01-09
Filing date: 2019-01-09
Publication date: 2021-07-30
Anticipated expiration: 2039-01-09
Also published as: CN109764516A

Abstract

The invention discloses an energy system, a control method thereof and a storage medium, and belongs to the field of energy. An energy system comprising a plurality of first heat conditioning devices and a plurality of second heat conditioning devices; the first evaporator of the first heat regulating device is communicated with the second evaporators of the plurality of second heat regulating devices in a heat exchange mode through a first medium distribution and mixing device; the first condensers of the first plurality of heat conditioning units are in heat exchange communication with the second condensers of the second plurality of heat conditioning units via a second media distribution and mixing device. According to the energy system provided by the embodiment of the invention, waste energy among different heat regulating devices is comprehensively utilized, so that the energy consumption and waste are reduced, and the energy conservation and emission reduction are realized. Specifically, heat exchange from the plurality of first heat regulating devices to the plurality of second heat regulating devices is realized.

Description

Energy system, control method thereof and storage medium

Technical Field

The present invention relates to the field of energy technologies, and in particular, to an energy system, a control method thereof, and a storage medium.

Background

In a general home environment, there are a plurality of home appliances, and the plurality of types of home appliances often have different functions and are all related to heat conversion. For example, when an indoor unit of an air conditioner is refrigerating, the outdoor unit can dissipate heat at the same time, and similarly, a water heater also needs to consume electric energy or dissipate heat when refrigerating, and on the other hand, the water heater needs to heat hot water and also consumes electric energy; in winter, the air conditioner needs to heat and can release part of cold energy. Some need heat, some give off heat, some need refrigeration, some give off cold volume, consequently, caused very big energy waste.

In the heating mode air conditioner, the condenser outputs heat for heating the indoor environment, and the evaporator outputs cold as waste cold to be dissipated through air. The evaporator of the refrigerator outputs cold for freezing or refrigerating food, and the condenser of the refrigerator outputs heat as waste heat to be dissipated through air. How to realize energy allocation between an air conditioner and a refrigerator, reduce energy consumption and waste and realize energy conservation and emission reduction is a problem to be solved urgently at present.

Disclosure of Invention

The embodiment of the invention provides an energy system, a control method thereof and a storage medium. The following presents a simplified summary in order to provide a basic understanding of some aspects of the disclosed embodiments. This summary is not an extensive overview and is intended to neither identify key/critical elements nor delineate the scope of such embodiments. Its sole purpose is to present some concepts in a simplified form as a prelude to the more detailed description that is presented later.

According to a first aspect of embodiments of the present invention, there is provided an energy source system comprising a plurality of first heat conditioning devices and a plurality of second heat conditioning devices; a first evaporator of the plurality of first heat conditioning units is in heat exchange communication with a second evaporator of the plurality of second heat conditioning units via a first medium distribution mixing device; the first condensers of the plurality of first heat conditioning units are in heat exchange communication with the second condensers of the plurality of second heat conditioning units via a second media distribution mixing device.

In an alternative embodiment, said first medium distributing and mixing device is arranged in series in a heat exchange communication between a first evaporator of a plurality of said first heat conditioning apparatuses and a second evaporator of a plurality of said second heat conditioning apparatuses; the second medium distribution mixing device is arranged in series on a communication path of heat exchange between the first condensers of the plurality of the first heat regulating devices and the second condensers of the plurality of the second heat regulating devices.

In an alternative embodiment, the first media distribution mixing device and the second media distribution mixing device comprise:

a plurality of intermediate heat exchangers, each intermediate heat exchanger comprising a first energy input and a first energy output;

one or more mixing units, each mixing unit having a plurality of second inputs, and, one or more second outputs; each mixing unit is respectively communicated with one first output end of the plurality of transfer heat exchangers through a second input end; and the combination of (a) and (b),

and the flow control valve is arranged on a pipeline of the first energy output end of the transit heat exchanger.

Wherein each of the intermediate heat exchangers is adapted to communicate with a first evaporator of one or more first heat conditioning devices via a first energy input; the second output end of each mixing unit is used for communicating with the second evaporator of one or more second heat regulating devices;

or each intermediate heat exchanger is used for being communicated with a first condenser of one or more first heat regulating devices through a first energy input end; the second output of each mixing unit is adapted to communicate with the second condenser of one or more second heat conditioning devices.

In an optional embodiment, the intermediate heat exchanger further includes a unidirectional heat conducting device, and the first energy input end and the first energy output end are disposed at two ends of the unidirectional heat conducting device.

In an alternative embodiment, the first media dispensing mixing device and the second media dispensing mixing device further comprise: the bypass transfer heat exchangers are arranged on the communication pipeline of the first energy input end of each transfer heat exchanger in parallel; wherein the bypass transit heat exchanger employs the transit heat exchanger as recited in claim 4.

In an alternative embodiment, the first and second media distribution mixing devices further comprise a switching device disposed at a connection interface where the first media distribution mixing device of claim 4 is connected in parallel for switching a communication path between the first evaporator and the second evaporator; and the switching device is arranged at the connection interface of the parallel connection of the second medium distribution mixing device of claim 4, and is used for switching the communication channel between the first condenser and the second condenser.

In an optional embodiment, the system further comprises a control device,

the control device is used for controlling the opening degree of a flow control valve of the first medium distribution and mixing device according to the temperatures of the first evaporators of the first heat regulating devices and the temperatures of the second evaporators of the second heat regulating devices;

and the control device is used for controlling the opening degree of a flow control valve of the second medium distribution and mixing device according to the temperatures of the first condensers of the first heat regulating devices and the temperatures of the second condensers of the second heat regulating devices.

According to a second aspect of the embodiments of the present invention, there is provided a control method of an energy system, including:

controlling the opening degree of a flow control valve of the first medium distribution and mixing device according to the temperatures of a first evaporator of the first heat regulating devices and the temperatures of a second evaporator of the second heat regulating devices;

and controlling the opening degree of a flow control valve of the second medium distribution and mixing device according to the temperatures of the first condensers of the plurality of first heat regulating devices and the temperatures of the second condensers of the plurality of second heat regulating devices.

In an optional embodiment, the control method further includes:

when the heat exchange between the first evaporator and the second evaporator cannot be performed in a set direction, a communication path for switching the heat exchange between the first evaporator and the second evaporator passes through the bypass transit heat exchanger in the first intermediate distribution and mixing apparatus according to claim 4;

when the heat exchange between the first condenser and the second condenser cannot be performed in a set direction, the communication path for switching the heat exchange between the first condenser and the second condenser passes through the bypass relay heat exchanger in the second intermediate distribution mixing device according to claim 4.

According to a third aspect of embodiments of the present invention, there is provided a storage medium having stored thereon a computer program which, when executed by a processor, implements the aforementioned control method of an energy system. The technical scheme provided by the embodiment of the invention has the following beneficial effects:

according to the energy system provided by the embodiment of the invention, waste energy among different heat regulating devices is comprehensively utilized, so that the energy consumption and waste are reduced, and the energy conservation and emission reduction are realized. Specifically, heat exchange from the plurality of first heat regulating devices to the plurality of second heat regulating devices is realized.

It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the invention, as claimed.

Drawings

The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments consistent with the invention and together with the description, serve to explain the principles of the invention.

Fig. 1 is a schematic diagram of an energy system according to an exemplary embodiment;

FIG. 2 is a schematic diagram of an energy system according to an exemplary embodiment;

FIG. 3 is a schematic diagram of an energy system according to an exemplary embodiment;

FIG. 4 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 5 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 6 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 7 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 8 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 9 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 10 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 11 is a schematic diagram of a construction of a relay heat exchanger according to an exemplary embodiment;

FIG. 12 is a schematic diagram illustrating the structure of a mixing unit according to an exemplary embodiment;

FIG. 13 is a schematic diagram illustrating the structure of a mixing unit in accordance with an exemplary embodiment;

fig. 14 is a schematic diagram of an energy system according to an exemplary embodiment;

fig. 15 is a block flow diagram illustrating a method of controlling an energy system in accordance with an exemplary embodiment;

fig. 16 is a block flow diagram illustrating a method of controlling an energy system according to an exemplary embodiment.

Detailed Description

The following description and the drawings sufficiently illustrate specific embodiments of the invention to enable those skilled in the art to practice them. Other embodiments may incorporate structural, logical, electrical, process, and other changes. The examples merely typify possible variations. Individual components and functions are optional unless explicitly required, and the sequence of operations may vary. Portions and features of some embodiments may be included in or substituted for those of others. The scope of embodiments of the invention encompasses the full ambit of the claims, as well as all available equivalents of the claims. Embodiments may be referred to herein, individually or collectively, by the term "invention" merely for convenience and without intending to voluntarily limit the scope of this application to any single invention or inventive concept if more than one is in fact disclosed. Herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other like elements in a process, method or apparatus that comprises the element. The embodiments are described in a progressive manner, each embodiment focuses on differences from other embodiments, and the same and similar parts among the embodiments are referred to each other. As for the methods, products and the like disclosed by the embodiments, the description is simple because the methods correspond to the method parts disclosed by the embodiments, and the related parts can be referred to the method parts for description.

Referring to fig. 1 to 14, illustrating a first aspect of an embodiment of the present invention, an energy system includes a plurality of first heat regulating devices 40 and a plurality of second heat regulating devices 50;

the first evaporator 41 of the first heat conditioning device 40 is in heat exchange communication with the second evaporator 51 of the second heat conditioning device 50 through a first medium distributing and mixing device;

the first condenser 42 of the first heat conditioning unit 40 is in heat exchange communication with the second condenser 52 of the second heat conditioning unit 50 via a second media distribution mixing device.

Wherein the first medium distributing and mixing device is used for transferring heat between the first evaporator 41 and the second evaporator 51, and the second medium distributing and mixing device is used for transferring heat between the first condenser 42 and the second condenser 52. The heat exchange between each first evaporator 41 and each second evaporator 51 is realized, and the cold exchange between each first condenser 42 and each second condenser 52 is realized.

Alternatively, as shown in fig. 1 and 2, the first heat regulating device 40 is an air conditioner in a heating mode, and the second heat regulating device 50 is a refrigerator. The cold energy output by the first evaporator 41 of the plurality of air conditioners 40 exchanges heat with the second evaporator 51 of the one or more refrigerators 50 through the first medium distribution mixing device, and is used for freezing or refrigerating foods stored in the refrigerators. The heat output from the second condenser 52 of the plurality of refrigerators 50 is heat-exchanged with the first condenser 42 of the one or more air conditioners 40 through the second medium-distributing mixing device for heating the indoor air. The air conditioner can be a household air conditioner, or a central air conditioning system of a building, or a central air conditioning system of a whole community, or other forms of air conditioners. The refrigerator may be a refrigerator product, a freezer, or other form of food freezing or refrigeration system. Of course, the first heat quantity adjusting apparatus 40 may be a refrigerator, and the second heat quantity adjusting apparatus 50 may be an air conditioner in a heating mode.

In an alternative embodiment, the energy system, as shown in fig. 1-3, includes a plurality of first heat regulating devices 40 and a plurality of second heat regulating devices 50. The heat exchange between the plurality of first evaporators 41 and the plurality of second evaporators 51 can be realized by using a medium distribution mixing device, as shown in fig. 2, wherein one first evaporator 41 supplies cold to one second evaporator 51, one first evaporator 41 supplies cold to the plurality of second evaporators 51, the plurality of first evaporators 41 supplies cold to the one second evaporator 51, and the plurality of first evaporators 41 supplies cold to the plurality of second evaporators 51. The heat exchange between the first condensers 42 and the second condensers 52 can be realized by a medium distribution mixing device, as shown in fig. 1, wherein one first condenser 42 supplies heat to one second condenser 52, one first condenser 42 supplies heat to the second condensers 52, the first condensers 42 supplies heat to the second condensers 52, and the first condensers 42 supplies heat to the second condensers 52.

In an alternative embodiment, as shown in fig. 1-14, a first media distribution mixing device and the second media distribution mixing device, collectively referred to as a media distribution mixing device, comprises:

a plurality of relay heat exchangers 20, each relay heat exchanger 20 comprising a first energy input 201 and a first energy output 202;

one or more mixing units 10, each mixing unit 10 having a plurality of second inputs 101, and one or more second outputs 102; each mixing unit 10 is respectively communicated with a first energy output end 202 of the plurality of intermediate heat exchangers 20 through a second input end 101; and the combination of (a) and (b),

and a flow control valve 11 provided in a communication line with the first energy output terminal 202 of each of the intermediate heat exchangers 20.

Wherein each intermediate heat exchanger 20 is adapted to communicate with the first evaporator 41 of one or more first heat conditioning devices 40 through a first energy input 201; the second output 102 of each mixing unit 10 is intended to communicate with the second evaporator 51 of one or more second heat conditioning devices 50;

alternatively, each intermediate heat exchanger 20 is adapted to communicate with the first condenser 42 of one or more first heat conditioning devices 40 through a first energy input 201; the second output 102 of each mixing unit 10 is adapted to communicate with the second condenser 52 of one or more second heat conditioning devices 50.

In the medium distribution mixing device of the present embodiment, the relay heat exchangers 20 are used to distribute the cold energy (or the heat energy on the second condenser 51 side) from the first evaporator 41 side, the mixing unit 10 mixes the different energies (heat energy or cold energy) distributed from the plurality of relay heat exchangers 20 to obtain the set energy, and the mixing unit 10 outputs the set energy to the second evaporator 51 (or the first condenser 42) corresponding to the set energy. The second evaporator 51 (or the first condenser 42) can be supplied with precisely matched energy. In particular, a medium of matching temperature may be provided.

The following describes the relay heat exchanger according to the embodiment of the present invention, with reference to fig. 4 to 11. The intermediate heat exchanger is divided into a first intermediate heat exchanger 20 and a second intermediate heat exchanger 30 according to whether the intermediate heat exchanger is provided with the unidirectional heat conduction device 31.

As shown in fig. 4 to 9, the first intermediate heat exchanger 20 includes,

a first energy input 201 for communicating with the first evaporator 41 of the one or more first heat conditioning devices 40 or the first condenser 42 of the one or more first heat conditioning devices 40;

a first energy output 202 for communication to one or more mixing units 10; and

and the conducting valves are arranged on the path of the first energy input end 201 and the path of the first energy output end 202.

In an alternative embodiment, the conducting valves include an input conducting valve 231 and an output conducting valve 232, the input conducting valve 231 is serially connected to the pipeline of the first energy input end 201, and the output conducting valve 232 is serially connected to the pipeline of the first energy output end 202. The purpose of the on-off valve is to control the opening or closing of the first energy input 201 and the first energy output 202. In a specific embodiment, an input end conduction valve 231 is disposed on the liquid inlet pipe and the liquid outlet pipe of each first energy input end 201 (each heat exchange device), and an output end conduction valve 232 is disposed on the liquid inlet pipe and the liquid outlet pipe of each first energy output end 202 (each heat exchange device). The opening and closing control, the flow control and the energy transfer regulation of the communication pipelines of the first energy input end 201 and the first energy output end 202 of the first intermediate heat exchanger 20 are respectively realized by controlling the respective conduction valves, and the heat exchange between the first heat regulation device 40 and the second heat regulation device 50 can be controlled according to actual conditions.

A first energy input terminal 201 for inputting the cooling energy (or the heating energy) of the first evaporator 41 (or the second condenser 52) side. The specific structure adopted is various, for example, a fluid medium is used as a carrier, the first energy input end 201 is communicated with the heat exchange device on the side of the first evaporator 41 (or the second condenser 52) through a pipeline by using a heat exchange device, the fluid medium absorbs cold (or heat) on the side of the first evaporator 41 (or the second condenser 52), the fluid medium flows to the first energy input end 201, and the first energy input end 201 exchanges heat with the medium fluid of the first energy output end 202, so that the energy is converted to the first energy output end 202.

In an alternative embodiment, the first energy input end 201 is embodied by a heat exchange device, such as a plate heat exchanger, an evaporator, or a heat exchange coil. The first energy output end 202 is specifically a heat exchange device, such as a plate heat exchanger, a condenser, or a heat exchange coil.

In the relay heat exchanger according to the embodiment of the present invention, the number of the first energy input ends 201 and the first energy output ends 202, and the arrangement of the external connection pipeline groups of the first energy input ends 201 and the first energy output ends 202 may be determined according to the number of the evaporators and the condensers on the connection side, and other factors.

In an alternative embodiment, the number of the first energy input ends 201 of the first intermediate heat exchanger 20 according to the embodiment of the present invention is one or more, and the piping of each first energy input end 201 is independently provided. For example, the first energy input 201 includes one (as shown in fig. 4, 5 and 9) or more (see the first energy output 202 of the relay heat exchanger 20 in fig. 7) third heat exchange devices, each of which has an inlet pipe 211 and an outlet pipe 212 (i.e., a group of communicating pipes 21), and is communicated with the first evaporator 41 through two pipes, specifically, with the first cold heat exchange device on the side of the first evaporator 41, or is communicated with the second condenser 52 through two pipes, specifically, with the second heat exchange device on the side of the second condenser 52. The cold on the side of the first evaporator 41 or the heat on the side of the second condenser 52 is transferred to the first energy input 201 by means of a fluid medium. That is, each third heat exchange means is independently communicated with each first evaporator 41 (or each second condenser 52). For another example, as shown in fig. 6 and 8, the first energy input end 201 is a third heat exchange device, and the liquid inlet end of the third heat exchange device is communicated with a plurality of liquid inlet pipes 211, and the liquid outlet end of the third heat exchange device is communicated with a plurality of liquid outlet pipes 212. One liquid inlet pipe 211 and one liquid outlet pipe 222 are formed as one communication pipe group 21 into a plurality of independent communication pipe groups, and are respectively communicated with each first evaporator 41 (or each second condenser 52) through the plurality of independent communication pipe groups.

In another alternative embodiment, the number of the first energy input ends 201 is multiple, and the pipelines of the multiple first energy input ends 201 are communicated with each other. There are many ways of communicating with each other, as long as it is achieved that a plurality of first energy input ends can all communicate with the first evaporator 41 of the first heat regulating device 40 or the first condenser 42 of the first heat regulating device 40. For example, as shown in fig. 7, the plurality of first energy input ends 201 are communicated with the liquid outlet transit pipe 222 through the liquid inlet transit pipe 221, the liquid inlet pipe 211 of each first energy input end 201 is communicated with the liquid inlet transit pipe 221, and the liquid outlet pipe 212 of each first energy input end 201 is communicated with the liquid outlet transit pipe 222. And then the liquid inlet transit pipeline 221 and the liquid outlet transit pipeline 222 are used as a communicating pipeline group and are communicated with the first evaporator 41 (or each second condenser 52) through two pipelines.

Similarly, when there are one or more first energy output ends 202, the pipeline of each first energy output end 202 is independently arranged in the same manner as the first energy input end 201. When there are a plurality of first energy output ends 202, the pipelines of the plurality of first energy output ends 202 are connected to each other in the same way as the first energy input end 201. And will not be described in detail herein.

In the first relay heat exchanger according to the embodiment of the present invention, the following specific embodiments are provided according to the arrangement manner of the pipelines of the first energy input end 202 and the heat exchange end 202.

As shown in fig. 4, in the first relay heat exchanger i, one first energy input end 201 is provided with a communicating pipe set; the number of the first energy output ends 202 is plural, and the communicating pipe groups of the plural first energy output ends 202 are independently arranged. That is, the first energy input 201 and the first energy output 202 are independently arranged in a pipeline. One path is converted into multiple paths.

As shown in fig. 5, in the first intermediate heat exchanger ii, there is one first energy input end 201, and there is one communicating pipe set; the number of the first energy output ends 202 is one, and one first energy output end 202 has a plurality of independently arranged communicating pipe groups. That is, the first energy input 201 and the first energy output 202 are independently arranged in a pipeline. One path is converted into multiple paths.

As shown in fig. 6, in the first relay heat exchanger iii, there is one first energy input end 201, and one first energy input end 201 has a plurality of independently arranged communicating pipe sets; the first energy output 202 is one, having one communicating tube bank. That is, the first energy input 201 and the first energy output 202 are independently arranged in a pipeline. And (4) converting the multiple paths into one path.

As shown in fig. 7, in the first intermediate heat exchanger v, the first energy input end 201 is plural, and the plural first energy input ends 201 are communicated with each other by a group of communicating tube sets to be communicated with the first evaporator 41 of the first heat regulating device 40 or the first condenser 42 of the first heat regulating device 40; the number of the first energy output ends 202 is plural, and the communicating pipe groups of the plural first energy output ends 202 are independently arranged. That is, the pipelines of the plurality of first energy input terminals 201 communicate with each other, and the pipelines of the plurality of first energy output terminals 202 are independently provided. One path is converted into multiple paths.

As shown in fig. 8, in the first intermediate heat exchanger iv, there is one first energy input end 201, and one first energy input end 201 has a plurality of independently arranged communicating pipe sets; the number of the first energy output ends 202 is one, and one first energy output end 202 has a plurality of independently arranged communicating pipe groups. That is, the first energy input 201 and the first energy output 202 are independently arranged in a pipeline. And (4) multiplexing the multiple paths.

As shown in fig. 9, in the first relay heat exchanger vi, there is one first energy input end 201, and there is one communicating pipe group; the first energy output 202 is one, having one communicating tube bank. That is, the first energy input 201 and the first energy output 202 are independently arranged in a pipeline. One path is changed into another path.

Of course, the structures of the first intermediate heat exchanger 20 according to the embodiment of the present invention are not limited to the above six, and the structures of the first energy input end 201 and the first energy output end 202 may be interchanged and may be combined arbitrarily. In practical application, the structure of the adaptive intermediate heat exchanger is selected. In addition, when the communication pipes of the first energy input end 201 (or the first energy output end 202) of the first intermediate heat exchanger 20 are formed into a plurality of sets, the number is not limited, and may be determined according to the number of the first evaporators 41 (or each second condenser 52) to be connected.

In the first relay heat exchanger 20 according to the embodiment of the present invention, the heat exchange device of the first energy input end 201 and the heat exchange device of the first energy output end 202 may be separately arranged, for example, when a plate heat exchanger is adopted, the two heat exchange devices are oppositely arranged (may be contacted or not contacted), so as to ensure that the heat exchange area is maximized; when the heat exchange coil is adopted, the coil parts of the heat exchange coil and the heat exchange coil are arranged in a staggered mode (can be contacted or not contacted), and effective heat exchange is guaranteed. Alternatively, the heat exchange device of the first energy input end 201 and the heat exchange device of the first energy output end 202 are designed as a whole. The arrangement is not limited, as long as the heat exchange device of the first energy input end 201 and the heat exchange device of the first energy output end 202 can perform heat transfer. As shown in fig. 4 to 9, the first energy input end 201 and the first energy output end 202 are both configured by contactless heat exchanging devices disposed oppositely, although the first intermediate heat exchanger according to the embodiment of the present invention is not limited to the configuration shown in the drawings.

The first energy input end 201 and the first energy output end 202 of the first intermediate heat exchanger 20 according to the embodiment of the present invention have the same structure when the heat exchange manner is the same, and the two energy input ends and the first energy output end can be used interchangeably, which is only defined for convenience of distinction.

As shown in fig. 10 and 11, the second intermediate heat exchanger 30 includes:

a first energy input end I301, which is used for communicating with the first evaporator 41 of one or more first heat regulating devices 40 or the first condenser 42 of one or more first heat regulating devices 40;

a first energy output I302 for communication to one or more mixing units 10; and the combination of (a) and (b),

the one-way heat conduction device 31, the first energy input end I301 and the first energy output end I302 are arranged at two ends of the one-way heat conduction device 31.

In the second intermediate heat exchanger 30 according to the embodiment of the present invention, by adding the unidirectional heat conducting device 31, when the first evaporator 41 exchanges cooling capacity with the second evaporator 51, more accurate cooling capacity transfer can be provided to the second evaporator 51 according to the target parameter (e.g., the target temperature) of the second evaporator 51. When supplying cooling energy to the second evaporator 51, the temperature of each fluid medium entering the mixing unit 41 can be precisely adjusted according to the temperature difference value between the target temperature and the actual temperature of the second evaporator 51, and the fluid medium with the set temperature can be precisely obtained by combining the flow control. In addition, the present invention is also applicable to a case where energy transmission in a predetermined direction is not possible between the first evaporator 41 and the second evaporator 51 (or between the second condenser 52 and the first condenser 42). In general, heat transfer is performed only from the higher temperature end to the lower temperature end, for example, if the heat exchange direction between the second condenser 52 and the first condenser 42 is set such that the second condenser 52 exchanges heat with the first condenser 42, and if the medium temperature itself on the second condenser 52 side is lower than the medium temperature itself on the first condenser 42 side, the heat exchange cannot be performed in the set direction, but rather, heat loss on the first condenser 42 side occurs, and the opposite effect is achieved. The same problem is encountered when cold is exchanged between evaporators. Therefore, the embodiment of the present invention provides the second intermediate heat exchanger 30, which utilizes the unidirectional heat conduction device 31 to adjust the medium temperature guided to the equipment from the heat (cold) storage station, so that it can provide accurate energy transfer; alternatively, the energy exchange can be performed normally in the set direction by the cold energy transfer between the first evaporator 41 and the second evaporator 51 and the heat energy transfer between the first condenser 42 and the second condenser 52.

In the second relay heat exchanger 30 according to the embodiment of the present invention, on the basis of the first relay heat exchanger 20, a unidirectional heat conducting device 31 is additionally arranged between the first energy input end and the first energy output end. Therefore, the first energy input terminal i 301 and the first energy output terminal i 302 of the second intermediate heat exchanger 30 are structurally configured and function the same as the first energy input terminal 201 and the first energy output terminal 202 of the first intermediate heat exchanger 20, and an input end conduction valve and an output end conduction valve are also respectively configured on the first energy input terminal i 301 and the first energy output terminal i 302, which are the same as the first intermediate heat exchanger 20. Reference is made to the foregoing for details, which are not repeated herein.

Therefore, according to the structures of the first transfer heat exchanger i to the first transfer heat exchanger vi as shown in fig. 4 to 9, the unidirectional heat conduction device 31 is added between the first energy input end and the first energy output end, and then the second transfer heat exchanger i to the second transfer heat exchanger vi with the first energy input end and the first energy output end corresponding to each other can be sequentially obtained. The second intermediate heat exchanger ii 30 shown in fig. 10 is obtained by adding the unidirectional heat transfer device 31 to the first intermediate heat exchanger ii 20, and the second intermediate heat exchanger vi 30 shown in fig. 11 is obtained by adding the unidirectional heat transfer device 31 to the first intermediate heat exchanger vi 20.

In the second intermediate heat exchanger 30 according to the embodiment of the present invention, the unidirectional heat conducting device 31 realizes (forcibly) heat exchange from the first energy input end i 301 to the first energy output end i 302. Specifically, a refrigerant heat exchanger or a semiconductor temperature regulator may be used.

In an alternative embodiment, as shown in fig. 10 and 11, the refrigerant heat exchanger includes an evaporator 311, a compressor (not shown), a condenser 312 and an expansion valve (not shown), which are connected to form a heat exchange loop. The second intermediate heat exchanger 30 includes two heat-absorbing chambers 303 and two heat-releasing chambers 304 which are arranged in a heat-insulating manner; the evaporator 311 is arranged opposite to the first energy input end i 301 of the second intermediate heat exchanger 30 and is arranged in the heat absorption chamber 303; the condenser 312 is disposed opposite to the first power output terminal i 302 of the second intermediate heat exchanger 30 and is disposed in the heat releasing chamber 304.

In another optional embodiment, the semiconductor temperature regulator comprises a semiconductor refrigeration piece, a first end heat exchanger arranged at a first end of the semiconductor refrigeration piece, a second end heat exchanger arranged at a second end of the semiconductor refrigeration piece, and a power supply device. The power supply device is used for supplying electric energy to the semiconductor refrigeration piece. By controlling the direction of the power supply current, the first end and the second end of the semiconductor refrigeration chip can be switched between two modes of heat generation and cold generation. For example, at a forward current, the first end is a cold end and the second end is a hot end; after the current direction is switched, the first end is switched to be the hot end, and the second end is switched to be the cold end. The second intermediate heat exchanger 30 includes two heat-absorbing chambers 303 and two heat-releasing chambers 304 which are arranged in a heat-insulating manner; the first end heat exchanger is arranged opposite to the first energy input end I301 of the second intermediate heat exchanger 30 and is arranged in the heat absorption chamber 303; the second end heat exchanger is disposed opposite to the first energy output end i 302 of the second intermediate heat exchanger 30 and is disposed in the heat release chamber 304. And determining that the first end heat exchanger is a hot end (or a cold end) and the second end heat exchanger is a cold end (or a hot end) according to actual conditions.

As shown in fig. 1 to 3, in the intermediate distribution and mixing apparatus, the intermediate heat exchanger is generally a one-to-multiple intermediate heat exchanger, wherein the number of multiple intermediate heat exchangers is consistent with the number of mixing units 10, and the intermediate heat exchanger is ensured to be capable of communicating with each mixing unit 10, i.e., supplying energy to each first heat regulating device (first condenser of air conditioner in heating mode) or second heat regulating device (second evaporator of refrigerator). Meanwhile, the relay heat exchanger may employ the aforementioned first relay heat exchanger 20 or second relay heat exchanger 30.

In the medium distribution and mixing apparatus according to the embodiment of the present invention, the mixing unit 10 is configured to mix media having different energies (temperatures) to obtain a medium having a set energy (set temperature), and then output the medium to the first heat regulating device 40 (or the second heat regulating device 50) side. Thus, in one embodiment, as shown in fig. 12 and 13, the mixing unit 10 has two separate chambers, one inlet chamber 110 and the other return chamber 120, the inlet chamber 110 having one or more inlet pipes 1011 and one or more outlet pipes 1012; the reflow chamber 120 has one or more input effluent pipes 1022 and one or more output influent pipes 1021. An input liquid inlet pipe 1011 and an input liquid outlet pipe 1022 constitute an input end communicating pipe group (i.e., the second input end 101), and an output liquid inlet pipe 1021 and an output liquid outlet pipe 1012 constitute an output end communicating pipe group (i.e., the second output end 102). One input end communication line group is communicated with one output end line group of the relay heat exchanger 20 (or 30), and one output end line group is communicated with the first heat adjusting device (or the second heat adjusting device) side, for example, the first condenser of the air conditioner in the heating mode, or the second evaporator of the refrigerator. The input end communication pipeline group of the mixing unit 10 is two or more, and is used for being communicated with the communication pipeline of the first energy output end of the two or more intermediate heat exchangers 20 (or 30). The output end of the mixing unit 10 may be connected to one or more sets of pipes, and when one set is used (fig. 12), the output end is connected to only one first condenser (or one second evaporator). In the case of multiple sets (fig. 13), the energy is supplied by communicating with multiple first condensers (or multiple second evaporators), respectively. And, at this moment, set up the switch valve on every output communicates pipeline group, make things convenient for opening and shutting of control part communicating pipe to the realization provides the energy for one or more attemperator.

Optionally, a switching valve 103 is disposed on a pipeline of the second input end 101 and the second output end 102 of the mixing unit 10, so as to facilitate the circulation of the control medium.

In an alternative embodiment, the medium distribution mixing device i comprises a plurality of first transit heat exchangers 20 for one-way transit and a plurality of mixing units 10; the plurality of communicating tube groups of the first energy output terminal 202 of each of the first intermediate heat exchangers 20 are respectively communicated to one communicating tube group of the second input terminals 101 of the plurality of mixing units 10. Specifically, two one-pass, multi-pass first intermediate heat exchangers 20 and two mixing units 10 are shown in fig. 1.

In an alternative embodiment, the medium distribution mixing device ii, a plurality of second transit heat exchangers 30 of one-way-multiple-way type and a plurality of mixing units 10; the plurality of communicating pipe sets of the first energy output end i 302 of each second type of intermediate heat exchanger are respectively communicated to one communicating pipe set of the second input ends 101 of the plurality of mixing units 10. Specifically, two one-pass, multi-pass second intermediate heat exchangers 30 and two mixing units 10 as illustrated in fig. 3.

In an alternative embodiment, as shown in fig. 14, the medium distribution mixing device iii further includes, on the basis of the medium distribution mixing device i, a bypass intermediate heat exchanger, which is disposed in parallel on the communication pipeline of the first energy input end 201 of each first intermediate heat exchanger 20 (which may be defined as a main-circuit intermediate heat exchanger); wherein the bypass relay heat exchanger adopts a second relay heat exchanger 30, and the main relay heat exchanger adopts a first relay heat exchanger 20.

In a further alternative embodiment, the medium distribution and mixing device iii further includes a switching device, and the structure of the switching device is not limited as long as the switching function is achieved. The switching device is arranged at a connecting interface of the second intermediate heat exchanger 30 of the medium distribution mixing device III which is connected in parallel through the parallel pipeline 310 and is used for switching a communication passage between the first evaporator 41 and the second evaporator 51; and a switching device is provided at a connection interface where the second relay heat exchanger 30 is connected in parallel, for switching a communication path between the first condenser 42 and the second condenser 52. The communication path between the first evaporator 41 and the second evaporator 51 and the communication path between the first condenser 42 and the second condenser 52 have two states, the first state is that they are in heat exchange communication with the mixing unit 10 through the first intermediate heat exchanger of the medium distribution mixing device iii, and the second state is that they are in heat exchange communication with the mixing unit 10 through the second intermediate heat exchanger 30, the first intermediate heat exchanger 20.

Alternatively, the switching device is a control valve set including two valves, a liquid inlet control valve 161 and a liquid return control valve 162, and switching of the communication path between the first evaporator 41 and the second evaporator 51 (or between the first condenser 42 and the second condenser 52) is realized by switching between a first state of blocking the parallel pipeline 310 of the second intermediate heat exchanger 30 and a second state of conducting the parallel pipeline 310 of the second intermediate heat exchanger 30 and blocking the first intermediate communication pipeline 210 of the parallel section of the second intermediate heat exchanger.

In an alternative embodiment, as shown in fig. 1 to 3, an energy system i comprises two first thermal conditioners 40 (air conditioners in heating mode) and two second thermal conditioners 50 (refrigerators). The first evaporators 41 of the two first heat regulating devices 40 are in heat exchange communication with the second evaporators 51 of the two second heat regulating devices 50 (refrigerators) through the medium distribution mixing device i (or the medium distribution mixing device ii); the two first evaporators 41 supply cooling energy to the two second evaporators 51. The first condensers 42 of the two first heat conditioning devices 40 are in heat exchange communication with the second condensers 52 of the two second heat conditioning devices 50 (refrigerators) via the medium distribution mixing device i (or the medium distribution mixing device ii); the two second evaporators 52 supply heat to the two first condensers 42.

In an alternative embodiment, the energy system ii comprises two first thermal conditioners 40 (air conditioners in heating mode) and two second thermal conditioners 50 (refrigerators). As shown in fig. 14, the first evaporators 41 of the two first heat regulating devices 40 are in heat exchange communication with the second evaporators 51 of the two second heat regulating devices 50 (refrigerators) through the medium distribution mixing device iii; the two first evaporators 41 supply cooling energy to the two second evaporators 51. The first condensers 42 of the two first heat conditioners 40 are in heat exchange communication with the second condensers 52 of the two second heat conditioners 50 (refrigerators) through the medium distribution mixing device iii; the two second evaporators 52 supply heat to the two first condensers 42.

In an alternative embodiment, the energy system further comprises a control device for controlling the opening degree of the flow control valve 11 of the first medium distribution and mixing device (medium distribution and mixing device i or medium distribution and mixing device ii) according to the temperatures of the first evaporators 41 of the plurality of first heat regulating devices 40 and the temperatures of the second evaporators 51 of the plurality of second heat regulating devices 50; and controlling the opening degree of the flow control valve 11 of the second medium distribution mixing device (medium distribution mixing device i or medium distribution mixing device ii) according to the temperatures of the first condensers 42 of the plurality of first heat quantity adjusting devices 40 and the temperatures of the second condensers 52 of the plurality of second heat quantity adjusting devices 50.

In the present embodiment, a control process (control method) of the control apparatus will be described by taking, as an example, the plurality of first evaporators 41 of two first heat quantity adjusting devices 40 (air conditioners in heating mode) and one second evaporator 51 of one second heat quantity adjusting device 50 (refrigerator). The flow control valve 11 is provided on the line of the first energy output end of the relay heat exchanger 20 (or 30), and can control the flow rate of each communicating line group. The required cooling capacity (e.g., the medium temperature) can be obtained according to the target temperature and the actual temperature of the second evaporator 51, and the cooling capacity is determined, i.e., the set temperature of the second output end of the mixing unit 10 corresponding to the second evaporator 51 can be determined. In general, the cold medium temperatures of the heat exchangers of the two first evaporators 41 are generally different, i.e. different cold medium temperatures of the first evaporators 41 can provide different cold. The set temperature is thus obtained by proportionally mixing the cold medium on the side of the two first evaporators 41, depending on the set temperature. The cold energy mediums at the two first evaporators 41 are mixed in proportion by controlling the opening degree of the flow control valve on the corresponding communication pipeline on the first energy output end of the transit heat exchanger. Similarly, when the plurality of first evaporators 41 are required to supply cooling capacity to the plurality of second evaporators 51, the set temperatures of the second output ends of the mixing units 10 corresponding to the second evaporators 51 are respectively determined, and the opening degree of the flow control valve on the corresponding communication pipeline on the first energy output end of the transfer heat exchanger correspondingly connected to each mixing unit 10 is determined according to the cooling capacity medium temperature of the heat exchange device on each first evaporator 41 side. For more details, reference may be made to the following section of the control method of the energy system.

With respect to the energy system ii described above, the control device is further configured to control to switch the communication between the first evaporator 41 and the second evaporator 51 (or between the first condenser 42 and the second condenser 52) and the first relay heat exchanger 20 through the second relay heat exchanger 30 when it is determined that the heat exchange between the first evaporator 41 and the second evaporator 51 (or between the first condenser 42 and the second condenser 52) cannot be performed in the set direction.

Specifically, the control process will be described taking the communication between the first condenser 42 and the second condenser 52 as an example. By detecting the second medium temperature on the second condenser 52 side (the heat medium temperature of the heat exchange device described below) and the first medium temperature on the first condenser 42 side (the set temperature described below), the relationship between the first medium temperature and the second medium temperature is determined, and whether or not heat exchange is possible between the first condenser 42 and the second condenser 52 in the set direction is determined. For example, the heat exchange direction is set such that heat is supplied from the second condenser 52 to the first condenser 42, and this is achieved on the premise that the second medium temperature on the second condenser 52 side is higher than the first medium temperature on the first condenser 42 side. Therefore, when the second medium temperature is lower than the first medium temperature, the heat exchange between the first condenser 42 and the second condenser 52 cannot be performed in the set direction, and at this time, the switching device is controlled so that the communication path for switching the heat exchange between the first condenser 42 and the second condenser 52 is communicated through the bypass relay heat exchanger (second relay heat exchanger 30) in the medium distribution mixing device iii. By analogy, the control principle of the cold quantity exchange between the first evaporator 41 and the second evaporator 51 is the same and will not be described again here. For more details, reference may be made to the following section of the control method of the energy system.

According to a second aspect of the embodiments of the present invention, there is provided a control method of an energy system, including,

s100, controlling the opening degree of a flow control valve of a first medium distribution and mixing device according to the temperatures of first evaporators of a plurality of first heat regulating devices and the temperatures of second evaporators of a plurality of second heat regulating devices;

and S200, controlling the opening degree of a flow control valve of the second medium distribution and mixing device according to the temperatures of the first condensers of the plurality of first heat regulating devices and the temperatures of the second condensers of the plurality of second heat regulating devices.

In the embodiment of the present invention, the first heat quantity adjusting device 40 is an air conditioner in a heating mode, and the second heat quantity adjusting device 50 is a refrigerator. The first evaporator 41 of the air conditioner is outdoors, discharging waste heat; the first condenser 42 is indoor, and heats the indoor. The second evaporator 51 of the refrigerator is in the refrigeration chamber of the refrigerator to refrigerate the food in the refrigeration chamber; the second condenser 52 is located outside the refrigerator and discharges waste heat.

Next, a control method of an embodiment of the present invention will be described by taking a plurality of first heat quantity adjusting apparatuses 40 (air conditioners in heating mode) and a plurality of second heat quantity adjusting apparatuses 50 (refrigerators) as examples.

In step S100, the temperature of the first evaporator 41 includes the cooling medium temperature (temperature of the discharged waste heat) on the first evaporator 41 side, and the temperature of the second evaporator 51 includes the target temperature and the actual temperature. The target temperature of the second evaporator 51 is set artificially, for example, -4 ℃. The actual temperature is the actual temperature inside the refrigerator.

Alternatively, taking the example of using the media distribution mixing device i, as shown in fig. 15, a step S100 is described, which includes:

s110, acquiring the cold quantity medium temperature of the heat exchange device at each first evaporator 41 side; acquiring a target temperature and an actual temperature of each second evaporator 51;

s120, determining substandard second evaporators 51 which need cooling capacity according to the target temperature and the actual temperature of each second evaporator 51; meanwhile, the temperature difference values of the substandard second evaporators 51 are obtained;

s130, obtaining a set temperature of the second output end 102 of each mixing unit 10 corresponding to each second evaporator 51 according to the temperature difference value;

s140, obtaining the input cold medium temperature of the first energy input end 201 of each first intermediate heat exchanger 20 correspondingly communicated according to the cold medium temperatures of the heat exchange devices on the sides of the plurality of first evaporators 41;

and S150, acquiring the opening degree of a flow control valve on a corresponding circulation pipeline group of a first energy output end of the first type intermediate heat exchanger 20 of the first medium distribution and mixing device I according to the set temperature of each mixing unit 10 and the input cold medium temperature of each first type intermediate heat exchanger 20.

In step S110, the cold medium temperature, the target temperature of the second evaporator 51, and the actual temperature can be obtained by the temperature sensor, respectively;

in step S120, the substandard second evaporator 51 is a second evaporator whose actual temperature does not reach the target temperature, specifically, the actual temperature is higher than the target temperature. The temperature difference value is the absolute value of the difference value between the target temperature and the actual temperature, and the larger the temperature difference value is, the more cold energy is required for reaching the target temperature.

In step S130, the setting of the set temperature is set according to the temperature difference, for example, the set temperature is the accumulation of the target temperature and the temperature difference, and the accumulation mode is different according to the amount of cold and the amount of heat. In this embodiment, the second evaporator side is cold, and therefore the set temperature is the target temperature desuperheating difference.

In S140, the opening degree of the conduction valve at the first energy input end of the first intermediate heat exchanger 20 is fully open, and the input refrigeration medium temperature at the first energy input end is positively correlated to the refrigeration medium temperature at the first evaporator 41 side.

In step S150, one second evaporator corresponds to one mixing unit 10, two or more first intermediate heat exchangers for energy input to the mixing unit 10 are determined according to the set temperature of the mixing unit 10, the ratio of the medium output from each first intermediate heat exchanger is determined according to the input cold medium temperature of the two or more first intermediate heat exchangers, and then the opening degree of the flow control valve on the corresponding circulation line group at the first energy output end of each first intermediate heat exchanger is determined.

Alternatively, the step S100 will be described by taking the medium distribution mixing device ii as an example, and the steps S110 to S130 are the same as the above. The subsequent steps are as follows:

s140', obtaining the input cold medium temperature of the first energy input end i 301 of each second intermediate heat exchanger 30 correspondingly communicated according to the cold medium temperatures of the heat exchange devices on the sides of the plurality of first evaporators 41;

s141, determining the heat exchange efficiency of the unidirectional heat conducting device 31 of the second transit heat exchanger 30 in the first medium distribution mixing device ii according to the set temperature of each mixing unit 10 and the input cold medium temperature and the set temperature of each second transit heat exchanger 30, and further obtaining the output cold medium temperature of the second energy output end i 302 of the second transit heat exchanger 30;

s150', the opening degree of the flow control valve on the corresponding flow pipeline group of the first energy output end i of the second intermediate heat exchanger 20 of the first medium distribution mixing device ii is obtained according to the set temperature of each mixing unit 10 and the output refrigeration medium temperature of each second intermediate heat exchanger 30.

In step S141, the heat transfer parameter is determined according to the correlation between the heat transfer efficiency of the unidirectional heat transfer device 31 and the heat transfer parameter after the unidirectional heat transfer device is turned on (see the content recorded in the control device), and the heat transfer efficiency is also determined, so that the temperature of the refrigerant medium output from the first energy output end is reduced, that is, the cooling capacity is increased, after the refrigerant medium input from the first energy input end of the second intermediate heat exchanger 30 is forcibly heat-exchanged by the unidirectional heat transfer device 31. Meanwhile, according to the set parameters, it is only required to ensure that the output cold medium temperature of at least one second intermediate heat exchanger 30 communicated with the corresponding mixing unit 10 is lower than the set temperature, and the output cold medium temperature of all the second intermediate heat exchangers 30 communicated with the corresponding mixing unit 10 cannot be lower than the set temperature.

In step S150', one second evaporator corresponds to one mixing unit 10, two or more second intermediate heat exchangers for energy input to the mixing unit 10 are determined according to the set temperature of the mixing unit 10, the ratio of the medium output from each first intermediate heat exchanger is determined according to the output cold medium temperature of the two or more second intermediate heat exchangers, and then the opening degree of the flow control valve on the corresponding circulation pipeline group at the first energy output end of each second intermediate heat exchanger is determined. With the second intermediate heat exchanger 30, the output cold medium temperature can be controlled precisely, providing precision in the energy supply.

Alternatively, step S100 will be described by taking the media distribution mixing device iii as an example, and steps S110 to S140 are the same as the above. Except that S150, only different steps are described below, specifically as follows:

s151', determining the set temperature of each mixing unit 10 and the input cold medium temperature of each first intermediate heat exchanger 20;

s152', when the set temperature is lower than the input cold medium temperature (i.e. it is determined that the first evaporator 41 and the second evaporator 51 cannot exchange heat in the set direction, and the set direction is that the first evaporator 41 supplies cold to the second evaporator 51), controlling the communication path of heat exchange between the first evaporator 41 and the second evaporator 51 to pass through the second intermediate heat exchanger; and performs step S153'. That is, the switching means is controlled to open the parallel line 310 of the second intermediate heat exchanger 30 and to block the communication line 210 of the parallel section of the second intermediate heat exchanger, so that the first evaporator 41 and the second evaporator 51 are in heat exchange communication with each other through the first intermediate heat exchanger 20 and the second intermediate heat exchanger 30.

When the set temperature is greater than the input cold medium temperature, step S150 ″ is performed.

S153', determining the heat exchange efficiency of the unidirectional heat conducting device 31 of the second transit heat exchanger 30 in the first medium distribution mixing device iii according to the set temperature of each mixing unit 10 and the input cold medium temperature and the set temperature of each second transit heat exchanger 30, and further obtaining the output cold medium temperature of the second energy output terminal i 302 of the second transit heat exchanger 30;

s154', the opening degree of the flow control valve on the corresponding circulation pipeline set of the first energy output end of the second intermediate heat exchanger 20 of the first intermediate distribution mixing device iii is obtained according to the set temperature of each mixing unit 10 and the output cold medium temperature of each second intermediate heat exchanger 20.

S150 ″, the opening degree of the flow control valve on the corresponding circulation pipeline group of the first energy output end of the first intermediate heat exchanger 20 of the first intermediate distribution mixing device iii is obtained according to the set temperature of each mixing unit 10 and the input cold medium temperature of each first intermediate heat exchanger 20.

In step S200, the temperature of the first condenser 42 includes a target temperature and an actual temperature, and the temperature of the second condenser 52 includes an ambient temperature (temperature of discharged waste heat) on the side of the second condenser 52. The target temperature of the first condenser 42 is set manually, for example, 24 ℃. The actual temperature is the actual temperature in the room.

Alternatively, taking the example of using the media distribution mixing device i, as shown in fig. 16, a step S200 is described, which includes:

s210, acquiring the heat medium temperature of the heat exchange device at each second condenser 52 side; acquiring a target temperature and an actual temperature of each first condenser 42;

s220, determining the substandard first condensers 42 which need heat supply according to the target temperature and the actual temperature of each first condenser 42; meanwhile, the temperature difference values of the substandard first condensers 42 are obtained;

s230, obtaining a set temperature of the second output end 102 of each mixing unit 10 corresponding to each first condenser 42 according to the temperature difference value;

s240, obtaining an input heat medium temperature of the first energy input end 201 of each first intermediate heat exchanger 20 correspondingly communicated according to the heat medium temperatures of the heat exchange devices at the sides of the plurality of second condensers 52;

and S250, obtaining the opening degree of the flow control valve on the corresponding circulation pipeline group of the first energy output end of the first type intermediate heat exchanger 20 of the second medium distribution and mixing device I according to the set temperature of each mixing unit 10 and the input heat medium temperature of each first type intermediate heat exchanger 20.

In step S210, the temperature of the thermal medium, the target temperature of the first condenser 42 and the actual temperature can be obtained by the temperature sensor respectively;

in step S220, the substandard first condenser 42 is a second evaporator whose actual temperature does not reach the target temperature, specifically, the actual temperature is lower than the target temperature. The temperature difference value is the absolute value of the difference between the target temperature and the actual temperature, and the larger the temperature difference value is, the more heat is required to reach the target temperature.

In step S230, the setting of the set temperature is set according to the temperature difference, for example, the set temperature is the accumulation of the target temperature and the temperature difference, and the accumulation mode is different according to the heat quantity and the cold quantity. In this embodiment, the first condenser side is the heat, and therefore, the set temperature is the target temperature warming differential.

In S240, the opening degree of the on-valve of the first energy input end of the first intermediate heat exchanger 20 is fully open, and the temperature of the heat medium input at the first energy input end is positively correlated to the temperature of the heat medium at the second condenser 52 side.

In step S250, one first condenser 42 corresponds to one mixing unit 10, two or more first intermediate heat exchangers for energy input to the mixing unit 10 are determined according to the set temperature of the mixing unit 10, the ratio of the medium output from each first intermediate heat exchanger is determined according to the input heat medium temperature of the two or more first intermediate heat exchangers, and then the opening degree of the flow control valve on the corresponding circulation pipeline group at the first energy output end of each first intermediate heat exchanger is determined.

Alternatively, step S200 will be described by taking the media distribution mixing device ii as an example, and steps S210 to S230 are the same as the above. The subsequent steps are as follows:

s240', obtaining the input heat medium temperature of the first energy input end i 301 of each second intermediate heat exchanger 30 correspondingly communicated with each other according to the heat medium temperature of the heat exchange devices at the sides of the plurality of second condensers 52;

s241, determining the heat exchange efficiency of the unidirectional heat conducting device 31 of the second intermediate heat exchanger 30 in the second intermediate distribution mixing device ii according to the set temperature of each mixing unit 10 and the input heat medium temperature and the set temperature of each second intermediate heat exchanger 30, and further obtaining the output heat medium temperature of the second energy output end i 302 of the second intermediate heat exchanger 30;

s250', obtaining the opening degree of the flow control valve on the corresponding flow pipeline group of the first energy output end i of the second intermediate heat exchanger 20 of the second medium distribution mixing device ii according to the set temperature of each mixing unit 10 and the output heat medium temperature of each second intermediate heat exchanger 30.

In step S241, the heat transfer parameter is determined according to the correlation between the heat exchange efficiency of the unidirectional heat transfer device 31 and the heat transfer parameter after the unidirectional heat transfer device is turned on (see the content recorded in the control device), and the heat exchange efficiency is also determined, so that the temperature of the heat medium output from the first energy output end i is increased, that is, the heat is increased, after the heat medium input from the first energy input end i of the second intermediate heat exchanger 30 is forcibly heat-exchanged by the unidirectional heat transfer device 31. Meanwhile, according to the setting parameters, it is only necessary to ensure that the output heat medium temperature of at least one second intermediate heat exchanger 30 communicated with the corresponding mixing unit 10 is higher than the setting temperature, and the output heat medium temperature of all the second intermediate heat exchangers 30 communicated with the corresponding mixing unit 10 cannot be lower than the setting temperature.

In step S250', a first condenser corresponds to a mixing unit 10, two or more second intermediate heat exchangers 30 for inputting energy to the mixing unit 10 are determined according to the set temperature of the mixing unit 10, the ratio of the medium output from each first intermediate heat exchanger 20 is determined according to the output heat medium temperature of the two or more second intermediate heat exchangers, and the opening degree of the flow control valve on the corresponding flow pipe group at the first energy output end of each second intermediate heat exchanger 30 is determined. With the second intermediate heat exchanger 30, the output heat medium temperature can be precisely controlled, providing precision in the energy supply.

Alternatively, step S200 will be described by taking the media distribution mixing device iii as an example, and steps S210 to S240 are the same as the above. Except that S250, only different steps are described below, specifically as follows:

s251', the magnitudes of the set temperature of each mixing unit 10 and the input heat medium temperature of each first intermediate heat exchanger 20 are determined;

s252', when the set temperature is higher than the input heat medium temperature (i.e. it is determined that the heat exchange between the second condenser 52 and the first condenser 42 cannot be performed in the set direction, and the set direction is the heat supply amount from the second condenser 52 to the first condenser 42), controlling the communication path of the heat exchange between the second condenser 52 and the first condenser 42 to pass through the second intermediate heat exchanger; and performs step S153'. That is, the switching means is controlled to open the parallel line 310 of the second intermediate heat exchanger 30 and to block the communication line 210 of the parallel section of the second intermediate heat exchanger, so that the second condenser 52 and the first condenser 42 are in heat exchange communication with each other through the first intermediate heat exchanger 20 and the second intermediate heat exchanger 30.

When the set temperature is less than the input heat medium temperature, step S250 ″ is performed.

S253', determining the heat exchange efficiency of the unidirectional heat conduction device 31 of the second intermediate heat exchanger 30 in the second intermediate distribution mixing device iii according to the set temperature of each mixing unit 10 and the input heat medium temperature and the set temperature of each second intermediate heat exchanger 30, and further obtaining the output heat medium temperature of the second energy output end i 302 of the second intermediate heat exchanger 30;

s254', the opening degree of the flow control valve on the corresponding flow pipeline group of the first energy output end i of the first intermediate heat exchanger 20 of the second medium distribution mixing device iii is obtained according to the set temperature of each mixing unit 10 and the output heat medium temperature of each second intermediate heat exchanger 20.

And S250', obtaining the opening degree of the flow control valve on the corresponding circulation pipeline group of the first energy output end of the first type intermediate heat exchanger 20 of the second medium distribution and mixing device III according to the set temperature of each mixing unit 10 and the input heat medium temperature of each first type intermediate heat exchanger 20.

According to a third aspect of embodiments of the present invention, there is provided a storage medium having a computer program stored thereon, characterized in that the computer program, when executed by a processor, implements the aforementioned control method of an energy system.

The present invention is not limited to the structures that have been described above and shown in the drawings, and various modifications and changes can be made without departing from the scope thereof. The scope of the invention is limited only by the appended claims.

Claims

1. An energy system comprising a plurality of first heat conditioning devices and a plurality of second heat conditioning devices;

a first evaporator when the plurality of first heat regulating devices are used for heating and a second evaporator when the plurality of second heat regulating devices are used for cooling are communicated in a heat exchange mode through a first medium distribution and mixing device;

a first condenser when the plurality of first heat regulating devices are used for heating and a second condenser when the plurality of second heat regulating devices are used for cooling are communicated in a heat exchange mode through a second medium distribution and mixing device;

the first and second media dispensing mixing devices comprising:

one or more mixing units, each mixing unit having a plurality of second inputs, and, one or more second outputs; each mixing unit is respectively communicated with a first energy output end of the plurality of transfer heat exchangers through a second input end; and the combination of (a) and (b),

the flow control valve is arranged on a pipeline of a first energy output end of the transit heat exchanger;

2. An energy system according to claim 1,

the first medium distribution mixing device is arranged on a communication path for heat exchange between first evaporators of a plurality of the first heat regulating devices and second evaporators of a plurality of the second heat regulating devices in series;

the second medium distribution mixing device is arranged in series on a communication path of heat exchange between the first condensers of the plurality of the first heat regulating devices and the second condensers of the plurality of the second heat regulating devices.

3. The energy system of claim 1, wherein said intermediate heat exchanger further comprises a unidirectional heat conducting device, and said first energy input and said first energy output are disposed at two ends of said unidirectional heat conducting device.

4. An energy system according to claim 1, wherein said first and second media distribution and mixing devices further comprise: the bypass transfer heat exchangers are arranged on the communication pipeline of the first energy input end of each transfer heat exchanger in parallel; wherein the bypass transit heat exchanger employs the transit heat exchanger as recited in claim 3.

5. An energy system according to claim 4, wherein the first and second media distribution/mixing devices further comprise a switching device provided at a connection interface where bypass transit heat exchangers of the first media distribution/mixing device are connected in parallel as recited in claim 4, for switching a communication path between the first and second evaporators;

the switching device is arranged at the connection interface of the bypass transfer heat exchanger of the second medium distribution mixing device connected in parallel as recited in claim 4, and is used for switching the communication passage between the first condenser and the second condenser.

6. An energy system according to claim 1 or 2, further comprising control means,

7. The control method of an energy system according to any one of claims 1 to 6, comprising:

8. The control method according to claim 7, the energy system being the energy system according to claim 4; the control method is characterized by further comprising the following steps:

when the heat exchange between the first evaporator and the second evaporator cannot be performed in a predetermined direction, the communication path for switching the heat exchange between the first evaporator and the second evaporator passes through the bypass relay heat exchanger in the first intermediate distribution/mixing device as recited in claim 4;

when the heat exchange between the first condenser and the second condenser cannot be performed in a predetermined direction, the communication path for switching the heat exchange between the first condenser and the second condenser passes through the bypass relay heat exchanger in the second intermediate mixing and blending device as set forth in claim 4.

9. A storage medium on which a computer program is stored, characterized in that the computer program realizes the control method of the energy system according to claim 7 or 8 when being executed by a processor.