TW201522879A - Multi-temperature multi-function system with compund controllable energy-saving module - Google Patents

Abstract

A multi-temperature multi-function system with compound controllable energy-saving module is disclosed, which comprises: a refrigeration/air-conditioning system, a warm liquid defrosting system, a superheat adjustment fluid storage module, a heat recovery system, a multi-temperature water system, a water circulation system. The refrigeration/air-conditioning system is provided for feeding a refrigerant to the warm liquid defrosting system for a deforesting process; the superheat adjustment fluid storage module is provided for controlling the temperature of the refrigerant; the heat recovery system is provided for control a heat recovery process; the multi-temperature water system is provided for a water temperature process so as to provide water flows of different temperatures; the water circulation system is provided for controlling a water circulating process to enable a circulation to be formed between the water circulation system and the heat recovery system, and thus enable water flows to circulate between the water circulation system and the heat recovery system.

Description

Multi-temperature domain multi-function system with controllable composite refrigeration air conditioning heat recovery energy-saving module

The invention relates to a multi-temperature multi-function system with a heat recovery energy-saving module of a controllable composite refrigeration air conditioner, in particular to a multi-temperature domain capable of improving power saving efficiency, recycling waste heat reuse, saving and environmental protection. Multi-function system.

For refrigeration systems, refrigeration systems or refrigerated air conditioning systems, most of them must be defrosted. At present, most of the defrosting devices adopt electric heating defrosting, and the electric defrosting consumes a high power, and the storage temperature is too high, which often causes variation in the quality of the frozen or refrigerated food.

In addition, the traditional hot gas defrosting will cause thermal shock, which is easy to malfunction in the future, and when the temperature is low, the defrosting temperature of the hot liquid defrosting will be too low. Although hydrothermal defrosting can be used, the refrigerant that is not completely condensed at the end of the condenser is introduced into the evaporator, so that the frost in the evaporator melts and falls due to the temperature rise, but in this way, when the temperature is too low, it is difficult to defrost and defrost. The time will be longer. The hot liquid defrosting and the hot gas defrosting must overcome the situation that the compressor is easy to be compressed by liquid. If the liquid gas separator is used to prevent the liquid from being compressed, the power consumption is large.

As for the heat recovery part, when the refrigeration system is not operating at a high rate in winter, the water temperature in the tank often fails to reach the set temperature. Moreover, the conventional heat recovery unit series condenser has a large pressure drop and is inefficient. The water circulation of the heat recovery hot water tank is also not properly energy-saving.

In addition, existing refrigeration systems, refrigeration systems, or refrigerated air conditioning systems are not capable of multi-temperature water use, and equipment must be purchased separately.

In one embodiment, the present invention provides a multi-temperature multi-function system with a controllable composite refrigeration air conditioning heat recovery energy-saving module, including a refrigerating air conditioning system, a warm liquid defrost assist system, and a superheat adjustment storage liquid. Module, a heat recovery system, a multi-temperature domain water outlet system and a circulating water auxiliary system; the refrigeration air conditioner sends the refrigerant to the warming defrosting auxiliary system for defrosting; the superheat adjustment liquid storage module is used for control The temperature of the refrigerant; the heat recovery system is used to control the heat recovery; the multi-temperature domain water system is used to control the water temperature to form water of different temperatures; the circulating water auxiliary system is used to control the water circulation, and the circulating water auxiliary system and the heat recovery system form a In the circuit, water can be circulated between the circulating water auxiliary system and the heat recovery system.

In order to make the reviewer have a better understanding and approval of the present invention, the detailed description is as follows.

1‧‧‧Multi-temperature multi-function system with controllable composite refrigeration air conditioning heat recovery energy-saving module

10‧‧‧Warm defrosting aid system

11‧‧‧ Temperature control valve

12‧‧‧ heat exchanger

13‧‧‧Defrost control valve

131‧‧‧Differential pipeline

14‧‧‧First evaporator

15‧‧‧First evaporative pressure regulating valve

20‧‧‧Superheat adjustment liquid storage module

21‧‧‧ first container

22‧‧‧Second container

30‧‧‧Heat recovery system

32‧‧‧heat recovery automatic controller

33‧‧‧First line

34‧‧‧Second line

35‧‧‧ third pipeline

36‧‧‧fourth pipeline

37‧‧‧First condenser

38‧‧‧First condensing pressure regulating valve

39‧‧‧Second condensing pressure regulating valve

40‧‧‧Multiple temperature field water system

41‧‧‧Water supply equipment

42‧‧‧Pre-cooled container

43‧‧‧ Ice water container

44‧‧‧Control valve assembly

441, 442, 443‧‧‧ control valves

46‧‧‧heat recovery unit

48‧‧‧ heat exchanger

50‧‧‧Circulating water auxiliary system

51‧‧‧Preheating container

52‧‧‧Insulation insulation container

53‧‧‧Hot water pump

54‧‧‧Water level switch

55A‧‧‧First Control Valve

55B‧‧‧Second control valve

55C‧‧‧third control valve

55D‧‧‧fourth control valve

56A‧‧‧First temperature controller

56B‧‧‧Second temperature controller

56C‧‧‧ third temperature controller

60‧‧‧Refrigeration system

61‧‧‧Compressor unit

62‧‧‧second condenser

63‧‧‧Expansion device group

64‧‧‧Second evaporator

65‧‧‧Second evaporative pressure regulating valve

1 is a block diagram of an embodiment of the present invention.

2 is a schematic structural view of an embodiment of a refrigerating and air-conditioning system of the present invention.

3 is a schematic structural view of an embodiment of a warm liquid defrosting assistance system of the present invention.

4 is a schematic structural view of an embodiment of a superheat degree adjusting liquid storage module of the present invention.

FIG. 5 is a schematic structural diagram of an embodiment of a heat recovery system of the present invention.

FIG. 6 is a schematic structural diagram of an embodiment of a multi-temperature domain water outlet system of the present invention.

FIG. 7 is a schematic structural view of an embodiment of a superheat degree adjusting liquid storage module of the present invention.

The technical means and efficacy of the present invention for achieving the object will be described below with reference to the accompanying drawings, and the embodiments set forth in the following drawings are only for the purpose of explanation, and are understood by the reviewing committee, but the technical means of the present invention are It is not limited to the illustrated figures.

Referring to FIG. 1 , the present invention provides a multi-temperature multi-function system 1 with a controllable composite refrigeration air conditioning heat recovery energy-saving module, which comprises a warm liquid defrosting auxiliary system 10 and a superheat adjustment liquid storage mold. The group 20, a heat recovery system 30, a multi-temperature domain water discharge system 40, a circulating water auxiliary system 50, and a refrigerating air conditioning system 60.

First, please refer to the schematic diagram of the structure of the embodiment of the refrigerating and air-conditioning system 60 shown in FIG. 2. The refrigerating and air conditioning system 60 includes a compressor unit 61, a second condenser 62, and an expansion The device group 63, the second evaporator 64, and a second evaporation pressure regulating valve 65. The compressor group 61 can be composed of a single compressor or a plurality of compressors. The expansion device group 63 can be constructed of at least two expansion valves. The compressor unit 61 can supply a refrigerant (not shown) to the second condenser 62, the expansion device group 63, and the second evaporator 64. The second evaporating pressure regulating valve 65 is disposed between the second evaporator 64 and the superheat adjusting liquid storage module 20 for adjusting the pressure of the refrigerant entering the superheat adjusting liquid storage module 20, but may be required according to actual needs. It is determined whether or not the second evaporation pressure adjustment valve 65 is provided.

Please refer to the schematic diagram of the embodiment of the warm liquid defrosting assistance system 10 shown in FIG. The warming defrosting assistance system 10 includes a temperature control valve 11, a heat exchanger 12, a defrosting control valve 13, a first evaporator 14, and a first evaporation pressure regulating valve 15. The temperature control valve 11 is connected to the outlet end of the compressor unit 61. The heat exchanger 12 is disposed between the temperature control valve 11 and the defrosting control valve 13, and the heat exchanger 12 may be an air-cooled heat exchanger or a water-cooled heat exchanger or a heat exchanger of any type. The defrosting control valve 13 is connected to the first evaporator 14, the first evaporator 14 is connected to the evaporation pressure regulating valve 15, and the evaporating pressure regulating valve 15 is connected to the superheat adjusting liquid storage module 20.

The warming liquid defrosting assistance system 10 can be used to control the defrosting. The working principle of the warming liquid defrosting auxiliary system 10 is that when the defrosting is started, the defrosting control valve 13 is opened, and most of the refrigerant can flow into the first through the branch line 131. The evaporator 14 can therefore be defrosted by flowing hot liquid refrigerant into the first evaporator 14.

When the temperature of the branch line 131 is lower than a certain set value, the temperature control valve 11 is opened to allow the high-pressure hot gas refrigerant to enter the branch line 131 to increase the temperature of the original liquid refrigerant to achieve the defrosting effect. If the temperature reaches a second predetermined temperature before the defrosting control valve 13 is detected, the temperature control valve 11 is immediately closed.

Since the heat exchanger 12 is appropriately added at an appropriate position between the branch line 131 and the outlet of the compressor unit 61, the temperature of the high-pressure hot gas refrigerant can be made not too high. The first evaporating pressure regulating valve 15 can adjust the pressure of the evaporating refrigerant entering the superheat adjusting liquid storage module 20. However, whether or not the first evaporation pressure regulating valve 15 is provided may be determined according to actual needs.

Please refer to the schematic diagram of the embodiment of the superheat adjustment liquid storage module 20 shown in FIG. The superheat adjustment liquid storage module 20 includes a first container 21 and a second volume The second container 22 is disposed in the first container 21, and the first container 21 communicates with an outlet of a first condenser 37 (part of the components of the heat recovery system 30) and an inlet of the expansion device group 63. The second container 22 is in communication with the inlet end of the compressor unit 61 and the outlet end of the first evaporator 14. The first container 21 provides high temperature refrigerant access and the second container 22 provides low temperature refrigerant access.

The superheat adjustment liquid storage module 20 can be used to control the temperature of the refrigerant. The working principle of the superheat adjustment liquid storage module 20 is that, in the case of defrosting and a sudden increase in flow rate, in order to avoid liquid compression, compression is performed. The inlet end of the machine 61 is provided with a superheat adjustment liquid storage module 20, and the high temperature refrigerant of the first container 21 is used to raise the temperature of the low temperature refrigerant of the second container 22 to maintain the outlet of the first evaporator 14 to the inlet end of the compressor unit 61. The degree of superheat does not cause liquid compression.

When the refrigerant is recirculated at a low temperature, the low-temperature refrigerant first enters the bottom of the second container 22, and is absorbed by the first container 21 to rapidly evaporate into a superheated gas, and then sent back to the compressor unit 61, so as to avoid liquid compression and breakage. The connecting rod and valve plate of the compressor unit 61. In addition, the superheat adjustment liquid storage module 20 itself has a power saving effect.

Please refer to the schematic diagram of the architecture of the embodiment of the heat recovery system 30 shown in FIG. The heat recovery system 30 includes a heat recovery automatic controller 32 having a first line 33, a second line 34, a third line 35, a fourth line 36, a first condenser 37, A first condensing pressure regulating valve 38 and a second condensing pressure regulating valve 39. The first line 33 is connected to the outlet end of the compressor unit 61, the second line 34 is connected to a heat recovery unit 46 (part of the multi-temperature domain water outlet system 40), and the third line 35 is connected to the first condenser. 37. The fourth conduit 36 is connected to the inlet end of the compressor unit 61. The first condensation pressure adjustment valve 38 is disposed between the first condenser 37 and the superheat adjustment reservoir module 20. The second condensing pressure regulating valve 39 is disposed between the heat recovery automatic controller 32 and the superheat adjusting liquid storage module 20.

The heat recovery system 30 can be used to control heat recovery. The heat recovery system 30 operates on the principle that when heat recovery begins, the heat recovery automatic controller 32 opens the second line 34, most of the refrigerant, especially the hot refrigerant. It will flow into the heat recovery unit 46 via the second line 34 for heat recovery.

When the hot water storage tank (that is, the heat insulating container 52 shown in Fig. 7) reaches the hot water When the temperature is set, the heat recovery automatic controller 32 opens the third line 35, and most of the refrigerant, especially the hot refrigerant, flows into the first condenser 37 via the third line 35 for heat dissipation.

When the above switching is performed, if the refrigerant flow rate suddenly increases, the heat recovery automatic controller 32 automatically discharges the pressure from the fourth line 36 to the low pressure side.

By using the heat recovery automatic controller 32, the refrigerant hot liquid at the outlet of the compressor unit 61 can be completely flowed into the heat recovery unit 46, in addition to ensuring sustainable heat recovery under the operation of the compressor unit 61, and the refrigerant hot liquid can be completely hot. The heat exchanger 46 performs heat exchange, and the efficiency is good, and the problem that the warm liquid defrosting is not easy to defrost when the temperature is too low can be improved.

Please refer to the schematic diagram of the architecture of the multi-temperature domain water outlet system shown in FIG. The multi-temperature domain water outlet system 40 includes a water supply device 41, a pre-cooling container 42, an ice water container 43, a control valve assembly 44, a heat recovery unit 46, and a heat exchanger 48. The water supply device 41 can supply water, the pre-cooling container 42 is for receiving water sent by the water supply device 41, the ice water container 43 is connected to the pre-cooling container 42, and the control valve assembly 44 is connected to the water supply device 41, the heat-insulating insulated container 52 and the ice. The water container 43, the heat recovery unit 46 is connected to the water supply device 41 and the preheating container 51, and the heat exchanger 48 is disposed between the pre-cooling container 42 and the water supply device 41. Since the multi-temperature domain water discharge system 40 is used with the warm liquid defrosting assistance system 10, the circulating water auxiliary system 50, and the refrigerating air conditioning system 60, the first evaporator 14 and the first of the warm liquid defrosting assistance system 10 are shown in FIG. The evaporation pressure regulating valve 15, the preheating container 51 of the circulating water auxiliary system 50, the adiabatic insulated container 52 and the hot water pump 53, and the compressor group 61 of the refrigerating and air-conditioning system 60, the expansion device group 63, the second evaporator 64, and the second evaporation Pressure regulating valve 65.

The multi-temperature domain water discharge system 40 can be used to control the water temperature. The multi-temperature domain water discharge system 40 operates on the principle that the refrigerant flows out of the compressor unit 61 and flows into the heat recovery unit 46. After the refrigerant flows out of the heat recovery unit 46, it flows into the expansion unit. 63. Since the expansion device group 63 has at least two expansion valves (not released), the high pressure refrigerant can be reduced to different low pressure cold coals, and then flow into the first evaporator 14 and the second evaporator 64, respectively. After passing through the first evaporation pressure adjusting valve 15 and the second evaporation pressure adjusting valve 65, the pressure is increased to the superheat adjusting liquid storage module 20, and then returned to the compressor unit 61.

Wherein, the water of the water supply device 41 flows through the heat recovery unit 46 to become hot water, and flows to the pre-heat The heat container 51 is then placed in an adiabatic insulated container 52 (which can be heated to the desired temperature in the field). If the water of the water supply device 41 flows into the ice water through the heat exchanger 46, it flows to the pre-cooling container 42, and then to the ice water container 43 (which can be cooled to the temperature required at the site). The hot water, ice water, and ambient water supplied by the water supply device 41 can be controlled to flow into the desired application environment by the control valves 441, 442, 443 of the control valve assembly 44, respectively.

Please refer to the schematic diagram of the structure of the superheat adjustment liquid storage module shown in FIG. The circulating water auxiliary system 50 includes a preheating container 51, an insulated thermal insulation container 52, a hot water pump 53, a water level switch 54, a first control valve 55A, a second control valve 55B, a third control valve 55C, and a The fourth control valve 55D, a first temperature controller 56A, a second temperature controller 56B, and a third temperature controller 56C. The preheating vessel 51 is connected to the heat recovery unit 46. The hot water pump 53 is disposed between the preheating vessel 51 and the heat recovery unit 46. The water level switch 54 is disposed between the first temperature controller 56A and the heat insulating and holding container 52 for measuring the water level of the heat insulating and holding container 52. The first control valve 55A is disposed between the preheating container 51 and the hot water pump 53, the second control valve 55B is disposed between the preheating container 51 and the heat insulating and holding container 52, and the third control valve 55C is disposed in the heat recovery unit 46 and insulated. Between the heat preservation containers 52, the fourth control valve 55D is disposed between the preheating container 51 and the heat recovery unit 46, and the first temperature controller 56A is disposed between the preheating container 51 and the first control valve 55A, and the second temperature control The 56B is disposed between the first control valve 55A and the hot water pump 53, and the third temperature controller 56C is disposed between the third control valve 55C and the fourth control valve 55D.

The circulating water auxiliary system 50 can be used to control the water circulation. The circulating water auxiliary system 50 works according to the principle that the water of the water supply device 41 flows into the heat recovery unit 46 and the second condenser 62 for heat exchange for preheating, and the preheated water flows into the preheating container. 51, the preheating container 51 can be insulated. When the water of the preheating container 51 reaches the set value of the first temperature controller 56A, the first control valve 55A and the second control valve 55B are opened, and the water of the preheating container 51 is It flows into the heat insulating container 52.

When the first control valve 55A is opened and the second control valve 55B is closed, only the water of the preheating container 51 is circulated.

When the first control valve 55A is closed and the second control valve 55B is closed, the water of the preheating container 51 and the water of the heat insulating container 52 are not circulated.

When the first control valve 55A is closed and the second control valve 55B is opened, and the water temperature of the heat recovery unit 51 is higher than the temperature of the third temperature controller 56C, the water of the heat insulating container 52 is circulated, and the water of the preheating container 51 is preheated. The water does not circulate until the temperature of the water is higher than the temperature of the second temperature controller 56B, and the water of the adiabatic insulated container 52 stops circulating. In order to achieve high-low temperature domain hot water, low temperature domain circulation water assisted energy saving effect.

Referring to FIG. 1 again, through the above detailed description of each architecture, the warming defrosting of the multi-temperature domain multi-function system 1 with the controllable composite refrigeration air conditioning heat recovery energy-saving module provided by the present invention can be summarized. The correlation between the auxiliary system 10, the superheat adjustment liquid storage module 20, the heat recovery system 30, the multi-temperature domain water discharge system 40, the circulating water auxiliary system 50, and the refrigerating air conditioning system 60, and the controllable by the present invention The main working principle of the multi-temperature multi-function system 1 of the composite refrigerating air-conditioning heat recovery energy-saving module is as follows: the refrigerating air-conditioning system 60 sends the refrigerant to the warming defrost assisting system 10 (path P1) to defrost the heating liquid. The auxiliary system 10 is used for defrosting; the refrigerant is sent to the heat recovery system 30 (path P2), and the heat recovery system 30 sends the refrigerant to the first condenser 37 and the heat recovery unit 46 (as shown in FIG. 5); The refrigerant passing through the first condenser 37 is sent to the superheat adjustment liquid storage module 20 (path P3), and the superheat degree adjustment liquid storage module 20 adjusts the temperature of the refrigerant to generate condensation gas, and the condensation gas is sent back to the refrigerating air conditioner. System 60 (path P4), then via cold The second evaporator 60 of the air conditioning system 64 into a multi-temperature water system domain 40 (path P5). The refrigerant passing through the heat recovery unit 46 can be heat recovered and sent to the multi-temperature domain water discharge system 40 (path P6).

As for the water in the multi-temperature zone water discharge system 40, it can be treated into water of different temperatures, for example, hot water, ice water and normal temperature water, for different situations.

The circulating water auxiliary system 50 is combined with the heat recovery system 30 to form a circulation loop, the circulating water auxiliary system 50 has an energy saving effect, and the heat recovery system 30 can produce hot water, and the water can be used in the circulating water auxiliary system 50 and the heat recovery system. 30 cycles (paths P7, P8).

In summary, the multi-temperature multi-function system with the heat recovery energy-saving module of the controllable composite type refrigerating air-conditioning system provided by the invention uses the refrigerant of the liquid pipe area at the end of the condenser Different control strategies for the overheating defrost assist system to improve the problem of conventional hydrothermal defrost methods are achieved by using heat exchangers and temperature control valves. And a superheat adjustment liquid storage module is arranged in front of the compressor unit to prevent liquid compression. At the outlet of the compressor unit, an automatic control valve for heat recovery is provided to keep the water temperature of the tank tank at the upper limit of the set value, thereby saving power consumption of electric heating, power consumption during operation, waste heat recovery, and maintaining the constant temperature of the tank. The heat recovery unit and the heat exchanger are used to combine the refrigeration system with the water supply equipment. The technology used is to make ice water from the water supply equipment through heat exchanger and cold air heat exchange. The supplied water is heated by a heat recovery unit and a condenser and a heater to produce hot water. The ice water flows into the pre-cooling container to keep cold, and the cold water, hot water and ice water are finally controlled by the control valve. By controlling the water circulation of the preheating container to improve the power saving efficiency, and recycling waste heat for reuse, the purpose of saving and environmental protection is achieved.

However, the above is only the embodiment of the present invention, and the scope of the present invention cannot be limited thereto; therefore, the simple equivalent changes and modifications made in accordance with the scope of the present invention and the contents of the specification should be It is still within the scope of the invention patent.

1‧‧‧Multi-temperature multi-function system with controllable composite refrigeration air conditioning heat recovery energy-saving module

10‧‧‧Warm defrosting aid system

20‧‧‧Superheat adjustment liquid storage module

30‧‧‧Heat recovery system

40‧‧‧Multiple temperature field water system

50‧‧‧Circulating water auxiliary system

60‧‧‧Refrigeration system

P1~P8‧‧‧ Path

Claims (10)

A multi-temperature multi-function system with a controllable composite refrigeration air-conditioning heat recovery energy-saving module, comprising: a refrigerating air-conditioning system; a warm liquid defrost auxiliary system for controlling defrost, the refrigerating air-conditioning system will be a refrigerant Sending to the warming defrosting auxiliary system; a superheat adjusting liquid storage module for controlling the temperature of the refrigerant; and a heat recovery system for controlling heat recovery, the refrigerant is discharged from the warm liquid defrosting auxiliary system And then sent to the heat recovery system; a multi-temperature domain water outlet system for controlling the water temperature to form at least two different temperatures of water; and a circulating water auxiliary system for controlling the water circulation, the circulating water assisting system and The heat recovery system forms a circuit in which water can be circulated between the circulating water auxiliary system and the heat recovery system; the heat recovery system separately sends the refrigerant to the heat recovery system and the multi-temperature domain water outlet system, through which The refrigerant of the heat recovery system is sent to the superheat adjusting liquid storage module, and the superheat adjusting liquid storage module adjusts the temperature of the refrigerant to generate a condensation gas, and then sends the condensation gas back to the The frozen air conditioning system is further sent to the multi-temperature domain water outlet system via the refrigerating air conditioning system, and the refrigerant passing through the multi-temperature domain water outlet system is heat-recovered in the multi-temperature domain water outlet system, and then sent to the multi-temperature domain water outlet system. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the first aspect of the patent application, wherein the refrigerating air-conditioning system comprises: a compressor unit connected to the warm liquid a frost assisting system, the superheat adjusting liquid storage module is connected to an inlet end of the compressor group; a second condenser is connected to the compressor group; and an expansion device group is connected to the second condenser, the overheating Adjusting the liquid storage module to communicate with the inlet end of the expansion device group; and a second evaporator disposed between the expansion device group and the superheat adjustment liquid storage module, wherein the refrigerant is fed by the compressor unit The second condenser, the expansion device The set and the second evaporator are further flowed into the superheat adjustment liquid storage module. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the second aspect of the patent application, wherein the second evaporator and the superheat adjustment liquid storage module are provided with a The second evaporation pressure regulating valve is configured to adjust the pressure of the refrigerant entering the superheat adjusting liquid storage module. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the first aspect of the patent application, wherein the warm-liquid defrost auxiliary system comprises: a temperature control valve connected to The chilling air conditioning system; a defrosting control valve; a heat exchanger disposed between the temperature control valve and the defrosting control valve; and a first evaporator disposed on the defrosting control valve and the overheating Adjusting between the liquid storage modules, the superheat adjustment liquid storage module is connected to the outlet end of the first evaporator. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the fourth aspect of the patent application, wherein the first evaporator and the superheat adjustment liquid storage module are provided with a The first evaporation pressure regulating valve. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the first aspect of the patent application, wherein the superheat adjustment liquid storage module comprises: a first container, which is connected The heat recovery system and the refrigerating air conditioning system; and a second container connected to the refrigerating air conditioning system and the warm liquid defrost assisting system, the second container being disposed in the first container. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the first aspect of the patent application, wherein the heat recovery system comprises: a heat recovery automatic controller; a first tube a road connected to the heat recovery automatic controller and the refrigerating air conditioning system; a second pipeline connected to the heat recovery automatic controller and the multi-temperature domain water outlet system; a third pipeline connected to the heat recovery automatic controller; a fourth pipeline connected to the heat Recycling an automatic controller and the refrigerating and air-conditioning system; a first condenser having an outlet end connected to the superheat-adjusting liquid storage module, the third line being connected to the first condenser; the heat recovery system to the refrigerant Sending to the first condenser, the refrigerant passing through the first condenser is sent to the superheat adjusting liquid storage module, and the superheat adjusting liquid storage module adjusts the temperature of the refrigerant to generate condensation gas, and then The condensed gas is returned to the refrigerating air conditioning system. a first condensing pressure regulating valve disposed between the first condenser and the superheat adjusting liquid storage module; and a second condensing pressure regulating valve disposed on the heat recovery automatic controller and the superheat adjusting storage Between the liquid modules. The multi-temperature domain multi-function system with the controllable composite refrigeration air-conditioning heat recovery energy-saving module according to the first aspect of the patent application, wherein the multi-temperature domain water discharge system comprises: a water supply device for supplying water; a heat recovery device connected to the water supply device and the circulating water auxiliary system, the heat recovery system sends the refrigerant to the heat recovery device for heat recovery, and the refrigerant is sent to the multi-temperature domain water outlet system; a cold container for receiving water sent by the water supply device; a heat exchanger disposed between the pre-cooling container and the water supply device; an ice water container connected to the pre-cooling container; and a control valve assembly And connected to the water supply device, the ice water container and the circulating water auxiliary system. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to the first aspect of the patent application, wherein the circulating water auxiliary system comprises: a preheating container connected to the plurality of a temperature domain water outlet system; an insulated thermal insulation container connected to the preheating vessel; a heat pump connected to the preheating vessel; a first control valve disposed between the preheating vessel and the hot water pump; a second control valve disposed in the preheating vessel and the insulated thermal insulation vessel a third control valve disposed between the multi-temperature domain water outlet system and the insulated thermal insulation container; a fourth control valve disposed between the preheating container and the heat recovery device; a temperature controller disposed between the preheating container and the first control valve; a second temperature controller disposed between the first control valve and the heat pump; and a third temperature controller, It is disposed between the third control valve and the fourth control valve. The multi-temperature multi-function system with the controllable composite refrigerating air-conditioning heat recovery energy-saving module according to claim 9, wherein the adiabatic insulated container has a water level switch, which is set in the first temperature control Between the device and the insulated thermal insulation container.