CN111219901A - Thermodynamic system for adjusting power change of water pump - Google Patents

Abstract

The invention provides a thermodynamic system for adjusting power change of a water pump, wherein a working surface is provided with a temperature sensor for detecting the environment temperature of the underground working surface, the water pump is arranged between a heat exchanger and an air cooler, and when the detected temperature is higher than a certain temperature, the amplitude of the power increase of the water pump is larger and larger along with the continuous rise of the detected temperature; when the detected temperature is lower than a certain temperature, the power of the water pump is continuously reduced with the continuous reduction of the detected temperature, and the power of the water pump is continuously reduced by a larger and larger amplitude. The invention adopts the change of the increasing and decreasing amplitude of the power of the water pump, can adopt the timely and rapid adjustment when the temperature is higher or lower than a certain value, increases the adjustment amplitude, and can rapidly recover the temperature to the normal temperature range.

Description

Thermodynamic system for adjusting power change of water pump

The application is a divisional application aiming at 09.04.2019, application number 2019102780975 and invention name 'a deep well mining thermodynamic system'.

Technical Field

The invention belongs to the technical field of heat exchangers, and particularly relates to a thermodynamic system for deep well mining.

Background

In the deep well mining process, the problem of underground thermal environment deterioration is very prominent. With the increase of the mining depth of the mine, after the mine enters the deep part, the working surface of the mine starts to be affected by high temperature, which not only restricts the safe production construction of the mine, but also threatens the health of miners. The "metallic and non-metallic mine safety regulations" of China stipulate: the air temperature of the mining working face of the production mine is not more than 26 ℃, the air temperature of the electromechanical equipment chamber is not more than 30 ℃, and the operation must be stopped when the air temperatures of the two working places are more than 30 ℃ and 34 ℃. At the same time, the mining process generates a large amount of temperature-stable mine wastewater due to the process requirements. Taking a gold mine as an example, the existing deep well operation area (the depth is more than 500 m) mainly takes ventilation cooling as main, the underground temperature is high (29 ℃), the relative humidity is high (more than 96%), the cooling effect is poor, and the thermal environment is very severe. In order to ensure the safe production of mines and the health of workers, effective measures must be taken pertinently to reduce the environmental temperature and control the high-temperature heat damage.

Deep well cooling technology adopted at home and abroad comprises: arranging a ventilation system and cooling clothes for workers, and additionally arranging a refrigerator on the ground or in the pit. There are problems that: the ventilation system has poor effect along with the increase of the operation depth; the cooling clothes cost of workers is high, and the operation process is inconvenient; the underground refrigerator has the problems of difficult heat extraction, poor cooling effect, high operating cost and the like caused by taking air as a heat dissipation medium.

The mode of passively strengthening heat exchange is to strictly prevent the fluid vibration induction in the heat exchanger from being changed into effective utilization of vibration, so that the convective heat transfer coefficient of the transmission element at low flow speed is greatly improved, dirt on the surface of the heat transfer element is restrained by vibration, the thermal resistance of the dirt is reduced, and the composite strengthened heat transfer is realized.

The rapid development of heat exchangers and related technologies has led to encouraging progress over the last several decades, but some long-standing unsolved problems have become more prominent. The induction vibration and the heat transfer surface area scale of the fluid in the heat exchanger are the outstanding problems which are acknowledged by the world and need to be solved urgently. The fluid-induced vibration can cause severe noise and damage to the heat transfer tube bundle, and fouling of the heat transfer tube bundle surface can cause huge energy and resource loss. It is not possible to completely prevent the vibration of the tube bundle in the heat exchanger, but it is not always effective to prevent the vibration by increasing the strength of the heat transfer tube bundle to avoid the damage and noise of the tube bundle. The mode of passive heat transfer enhancement is to utilize the vibration of the fluid-induced heat transfer tube bundle to realize the heat transfer enhancement, and through the effective utilization of the vibration, the heat transfer enhancement can be realized while inhibiting the heat transfer surface scale deposit, the thermal resistance of the scale is reduced, and the composite heat transfer enhancement is realized.

Therefore, the invention provides a new mining circulating refrigeration system aiming at the defects of the existing deep well underground centralized refrigeration system, and simultaneously provides a novel heat exchanger to replace an evaporator and a condenser of a conventional refrigerator, and certain improvement is carried out on the original system.

Disclosure of Invention

In order to achieve the purpose, the invention adopts the following technical scheme:

a heat exchange system for intelligently controlling the temperature of a working area is characterized by comprising a heat exchanger and an air cooler, wherein the air cooler is arranged on a working surface part; the air cooler is characterized in that a temperature sensor is arranged on a working surface and used for detecting the environmental temperature of the underground working surface, a water pump is arranged between the heat exchanger and the air cooler, and the controller controls the power of the water pump according to the detected temperature of the temperature sensor.

Preferably, when the downhole temperature is higher than a set value, the power of the water pump is increased, and the flow of water flowing through the air cooler is increased; when the underground temperature is lower than a set value, the power of the water pump is reduced, and the flow of water flowing through the air cooler is reduced; when not in downhole operation, the water pump is turned off.

Preferably, the heat exchanger is provided with an elastic tube bundle assembly, and the fluid exchanges heat with water from the air cooler in the elastic tube bundle assembly.

A thermodynamic system for deep well mining comprises an air cooler, an evaporator, an expansion valve, a compressor, a condenser and a heat storage water tank, and is characterized in that the air cooler is used for cooling air entering underground, and the evaporator, the expansion valve, the compressor and the condenser are located underground to form a refrigerating system; the heat storage water tank is positioned on the ground; the water enters the evaporator through the pipeline after exchanging heat with the air in the air cooler, exchanges heat with the refrigerant in the evaporator, the refrigerant enters the condenser after being compressed by the compressor after absorbing heat, exchanges heat with the water from the heat storage water tank in the condenser after exchanging heat, and then returns to the evaporator after passing through the expansion valve.

Preferably, refrigerant tubes are provided in the evaporator and/or condenser, the refrigerant tubes being an elastic tube bundle assembly.

Preferably, the air cooler is a spray-type air cooler.

Preferably, a temperature sensor is arranged underground and used for detecting the underground environment temperature, a water pump is arranged between the evaporator and the air cooler, and the controller controls the power of the water pump according to the detected temperature of the temperature sensor.

When the underground temperature is higher than a set value, the power of the water pump is increased, and the flow of water flowing through the air cooler is increased; when the underground temperature is lower than a set value, the power of the water pump is reduced, and the flow of water flowing through the air cooler is reduced; when not in downhole operation, the water pump is turned off.

Preferably, the hot water storage tank is connected with a living area and supplies water to the living area, and the system further comprises an electric boiler which is started when the hot water production amount of the hot water storage tank is insufficient.

Preferably, the waste water is settled and chemically treated in the mine waste water pond, and can become bathing or domestic water at 40-50 ℃ after the heat storage water tank is heated.

Preferably, the elastic tube bundle assembly comprises a plurality of coil pipes, an inlet vertical pipe and an outlet vertical pipe, each coil pipe comprises a plurality of arc-shaped heat exchange tubes, the end parts of the adjacent heat exchange tubes are communicated, the plurality of heat exchange tubes form a series structure, the end parts of the heat exchange tubes form the free ends of the heat exchange tubes, the inlet vertical pipe is connected with the inlet of the first heat exchange tube, the outlet vertical pipe is connected with the outlet of the last heat exchange tube, the elastic tube bundle assembly is characterized in that the inlet vertical pipe is connected with the inlet of the first heat exchange tube through a pulsating tube, and the inlet of the inlet vertical pipe is connected with a pulsating flow generation device and.

Preferably, the pulse pipe is connected with the inlet of the first heat exchange pipe from the inlet vertical pipe in an inclined and upward manner.

Preferably, the pulse pipe is connected with the inlet stand pipe in a welding mode.

The invention has the following advantages:

1) the invention realizes the effect of intelligently controlling the temperature of the working surface by automatically adjusting the heat exchange quantity of the fluid according to the change of the temperature.

2) The invention provides a deep well mining heat management system based on water circulation, namely water is adopted as a circulating medium, the mode can realize the cooling of a cold end stope, and a hot end provides domestic hot water, so that the deep well mining heat management system has the advantages of high heat efficiency, long transmission distance, compact equipment and good safety, and is very suitable for deep well operation.

3) The refrigeration pipe adopted by the invention adopts the pulse pipe elastic pipe bundle, the inlet vertical pipe is connected with the inlet of the first heat exchange pipe through the pulse pipe, and the independent pulse pipe is omitted, so that the inlet vertical pipe and the pulse pipe are combined into a whole, and the technical effects of simple structure, convenience in control and high heat exchange efficiency are realized.

4) According to the invention, the elastic tube bundle heat exchange assemblies are arranged in a central annular distribution manner, so that the heat exchange effect is further improved, and the scaling is reduced.

5) The invention reasonably distributes and optimizes the pulsating flow in the plurality of pulsating tube bundle heat exchange assemblies in the coil according to different positions, thereby further improving the technical effect of pulsating heat exchange. And provides an optimal reference for the design of the evaporator or the condenser with the structure.

6) According to the invention, the circulating pipelines of the evaporator and the condenser are improved, so that pulsating flow can be intelligently generated according to actual needs, the size of the pulsating flow and the size of normal flow can be controlled, and the actual needs can be met.

Description of the drawings:

FIG. 1 is a schematic flow chart of the system.

Fig. 2 is a schematic diagram of a preferred evaporator configuration.

Fig. 3 is a schematic diagram of the pulsating coil arrangement of the present invention.

Fig. 4 is a schematic view of a pulsating flow generating device of the present invention.

Figure 5 is a schematic of the pulsating coil assembly of the present invention.

Fig. 6 is a schematic of an evaporator or condenser of the present invention incorporating a pulsing coil.

Fig. 7 is a schematic top view of an evaporator or condenser with a built-in pulse coil of the present invention.

Fig. 8 is a schematic diagram of the size structure of the heat exchange assembly inside the evaporator or the condenser of the invention.

Fig. 9 is a schematic flow chart of the system for arranging the hot water storage tank.

Fig. 10 is a schematic view of a structure for generating a pulsating flow in a condenser.

Fig. 11 is a schematic view of a structure for generating a pulsating flow in an evaporator.

In the figure: 1. the system comprises a compressor, 2, an evaporator, 3, an expansion valve, 4, a condenser, 5, a chilled water pump, 6, an air cooler, 7, a cooling water circulating pump, 8, a cooling tower, 9, chilled water, 10, a refrigerant, 11, cooling water outlet water, 12, cooling water inlet water, 13, air return shaft inlet air, 14 and air return shaft outlet air; 15. the refrigerating system comprises a shell, 16, an inner partition plate, 17, a chilled water inlet pipe, 18, a chilled water outlet pipe, 19, a refrigerant inlet pipe, 20, a refrigerant outlet pipe, 21, a spiral pipe, 22, a joint, 23, a seal head, 24 and a flange.

25. The tank 26, the shell side outlet 27, the shell side inlet 28, the pulsating coil assembly 29, the support, 30-34 the pulsating coil assembly 35, the counterweight 36, the pulsating coil 37, the pulse pipe 38, the tube side inlet standpipe 39, the heat exchange pipe 40, the counterweight 41, the tube side outlet standpipe 42, the electromagnetic pump 43, the main circuit valve 44, the bypass valve 45, the heat storage water tank 46, the electromagnetic pump 47, the main circuit valve 48 and the bypass valve.

Detailed Description

Fig. 1 shows a schematic diagram of the overall structure of a thermal system for deep well mining. As shown in fig. 1, the thermodynamic system for deep well mining comprises three parts, namely a return air shaft part, an underground chamber part and a working surface (mining area) part, wherein the return air shaft part is provided with a cooling tower 8, the underground chamber part is provided with an evaporator 2, an expansion valve 3, a compressor 1 and a condenser 4, and an air cooler 6 is arranged on the working surface part. The air cooler 6 is used for cooling down-hole air, and the evaporator 2, the expansion valve 3, the compressor 1 and the condenser 4 form a refrigerating system; the cooling tower 8 and the condenser 4 form a circulating pipeline, air of the return air shaft exchanges heat with water in the cooling tower 8, the water enters the condenser 4 through the pipeline and exchanges heat with a refrigerant in the condenser 4, the refrigerant enters the evaporator 2 after being subjected to heat release through the expansion valve 3, exchanges heat with water from an air cooler in the evaporator 2 and then returns to the condenser 4 through the compressor 1; the evaporator 2 and the air cooler 6 form an air cooler circulation pipeline, and water in the air cooler 6 exchanges heat with air on a working surface and then circulates to the evaporator 2 to exchange heat.

The invention provides a deep well mining heat management system based on water circulation, which is characterized in that water is used as a circulating medium, a refrigeration system, an air cooler and a cooling tower are arranged, and the air cooling arrangement of a return air shaft is fully utilized, so that underground temperature control can be well realized, and the purpose of safety is achieved. The mode can realize cold end stope cooling, has the advantages of high thermal efficiency, long transmission distance, compact equipment and good safety, and is very suitable for deep well operation.

Preferably, a water pump 5 is arranged in a circulating pipeline formed by the evaporator 2 and the air cooler 6, a temperature sensor is arranged in the working face and used for detecting the air temperature of the mining area, the water pump 5 and the temperature sensor are in data connection with a controller, and the controller controls the power of the water pump according to the detected temperature of the temperature sensor. When the temperature of the working surface is higher than a set value, the controller controls the power of the water pump 5 to increase, and the flow of water flowing through the air cooler is increased; when the temperature of the working surface is lower than a set value, the controller controls the power of the water pump to be reduced, and the flow of water flowing through the air cooler is reduced; when not in downhole operation, the water pump is turned off.

Through the power of intellectual detection system temperature and intelligent control water pump, can the temperature of intelligent control working face, avoid the high temperature or cross lowly, play fine intelligent control's effect.

Preferably, when the detected temperature is higher than a certain temperature, preferably higher than 25 degrees celsius, the power of the water pump increases with the rising of the detected temperature.

Preferably, when the detected temperature is lower than a certain temperature, preferably lower than 5 degrees celsius, the power of the water pump is reduced more and more along with the continuous reduction of the detected temperature.

The change of the increase and the reduction of the power of the water pump is adopted, so that the temperature can be quickly adjusted in time when the temperature is higher than or lower than a certain value, the adjustment amplitude is increased, and the temperature can be quickly restored to a normal temperature range.

Preferably, the air cooler is a spray-type air cooler.

Preferably, the water in the air cooler is sourced from mine water burst, and the mine water burst is subjected to precipitation and chemical treatment and then enters the evaporator 2 for heat exchange.

As a preferred embodiment, the structure of fig. 1 may be modified to use a high thermal storage tank 45 instead of the cooling tower 8, as shown in fig. 8, and water in the thermal storage tank is circulated back to the thermal storage tank after entering the condenser 4 and absorbing heat in the condenser 4.

Through setting up the hot water storage tank, can realize that the hot junction provides the function of life hot water, have the advantage that the thermal efficiency is high, transmission distance is far away, equipment is compact, the security is good, especially adapted deep well operation is used.

Preferably, the hot water storage tank is connected with a living area and supplies water to the living area, and the system further comprises an electric boiler which is started when the hot water production amount of the hot water storage tank is insufficient. By arranging the electric boiler, the requirement of domestic hot water can be automatically supplemented.

Preferably, the refrigerant 10 and the chilled water 9 exchange heat in the evaporator 2 to generate low-temperature chilled water, and the chilled water flows into the spray-type air cooler 6 through a pipeline to exchange heat with hot and humid air in a stope to generate low-temperature air, so that the purposes of cooling and dehumidifying are achieved. Because the quality of underground air is poor and the underground air contains a large amount of floating and sinking, secondary water of sprayed chilled water is seriously polluted, and therefore the secondary water is not recycled and is directly discharged from an air cooler, so that the chilled water can not be circulated, the evaporator 2 needs to continuously supplement inflow water, and the inflow water of the part is planned to adopt mine water gushing after precipitation and chemical treatment.

On the side of the condenser 4, cooling water inlet water 11 exchanges heat with a refrigerant 10 in the condenser to generate cooling water outlet water 12 with the temperature of 40-50 ℃, and the cooling water outlet water 12 is cooled by a cooling tower to complete the circulation of the cooling water.

In the aspect of equipment arrangement, the air cooler 6 is arranged in the working face of each underground stope and can move according to the change of the working face, and the conveying between the air cooler 6 and the evaporator 2 of the refrigerating unit is realized through the chilled water circulating pump 5; the cooling tower 8 is arranged at the side of a total return air well of the mine ventilation system, so that the heat of cooling water is taken away by the mine return air, and the power transmission of the cooling water is realized through a cooling water circulating pump 11; in addition to the air cooler 6 and cooling tower 8, other components of the overall system are disposed in a downhole chamber.

Preferably, a refrigerant pipe is provided in the evaporator and/or the condenser, and the refrigerant pipe is a spiral tube bundle assembly.

As a preferred embodiment of the spiral tube bundle assembly, the structure of the novel spiral coil heat exchange device of the evaporator of the refrigerator is described as the structure of a condenser, and the structure of the novel spiral coil heat exchange device is the same as that of the evaporator of the refrigerator, as shown in figure 2.

The spiral wound tube type heat exchanger is formed by alternately winding heat transfer tubes in a spiral shape in a space between a core barrel and an outer barrel, and 3-5 distance pieces in a certain shape are adopted for the adjacent two layers of spiral heat transfer tubes to keep a certain distance. The annular closed space formed by the outer cylinder, the core cylinder and the tube plate of the heat exchanger is the shell side space. If all the heat transfer tubes pass through the same medium, it is called a single-channel spiral-wound tube heat exchanger.

A group of heat exchange elements of the novel spiral coil heat exchanger in the design temporarily adopt three layers of spiral pipes 21, wherein the minimum diameter of a core cylinder is determined by the minimum curvature radius required by the innermost heat exchange pipe not being flattened in the winding theoretically, and the diameter of a common core cylinder is 160-360 millimeters. Although the chilled water is mine water burst after precipitation and chemical treatment, the water burst still contains more impurities and chemical substances, which have great adverse effect on the long-term use of the heat exchanger, so that the spiral coil is made of titanium alloy materials for improving the corrosion resistance.

Compared with a common single-channel spiral wound tube type heat exchanger, each layer of spiral tubes of the heat exchanger are mutually independent, each layer is formed by winding a titanium alloy pipeline, a refrigerant flows into three layers of spiral coils simultaneously through the diversion of a water collecting pipe above the refrigerant, the refrigerant flows in from a refrigerant inlet 17 and flows out from a refrigerant outlet 18, chilled water flows in from a chilled water inlet 19 and flows out from a chilled water outlet 20, and therefore the refrigerant in each layer of spiral coils and shell side chilled water can be ensured to be subjected to countercurrent heat exchange, and the heat exchange effect is improved.

The novel spiral coil heat exchanger has the advantages that vibration can be generated automatically in the using process, and the effects of enhancing heat transfer and weakening corrosion are achieved. Because each group of heat exchange elements are not provided with other fixed supporting points except the connection with the refrigerant inlet pipe and the refrigerant outlet pipe, when fluids with different pressures flow inside and outside the pipes respectively, the spiral coil pipe can vibrate under the action of gravity and flow, thereby strengthening the heat transfer and corrosion resistance.

In this design, a heat exchange unit comprises four groups of spiral coil pipes, if a group of spiral coil pipes breaks down, then can pull down the whole group of coil pipes by flange 24 department and overhaul, then seal flange 24 department, do not influence other three groups of coil pipes and normally work. The three-layer spiral pipe structure is known by the arrangement form and high heat exchange coefficient of the heat exchange pipes, the volume of the three-layer spiral pipe structure can be greatly reduced under the condition of the same heat exchange quantity, and the three-layer spiral pipe structure has great significance under a well with limited space. Because the refrigerator volume mainly embodies on evaporimeter and condenser volume, consequently adopt the refrigerator volume of novel spiral coil heat exchanger in this patent will dwindle greatly to be applicable to centralized refrigerating system in pit more.

As a preferred embodiment, the refrigerant tubes are an elastic tube bundle assembly, as shown in fig. 3-6.

Fig. 3 to 5 show a pulsating tube bundle heat exchange assembly 30, which comprises a plurality of coil pipes 30, inlet riser pipes 38 and outlet riser pipes 41, wherein the plurality of coil pipes 30 are arranged along the height direction as shown in fig. 3, each coil pipe 30 comprises a plurality of heat exchange pipes 38 in the shape of a circular arc, the ends of the adjacent heat exchange pipes 38 are communicated, so that the plurality of heat exchange pipes 38 form a series structure, and the ends of the heat exchange pipes form the free ends of the heat exchange pipes (the position of the bearing block is arranged in fig. 3), the plurality of heat exchange pipes are distributed along the same circle center from the circle center to the outside in sequence, the inlet riser pipe 38 is connected with the inlet of the outermost heat exchange pipe, the outlet riser pipe 41 is connected with the outlet of the innermost heat exchange pipe 38, the inlet riser pipe 38 is connected with the inlet of the outermost heat exchange pipe through a pulsating tube 37, the inlet, thereby further promoting the vibration of the elastic heat exchange tube bundle to carry out enhanced heat transfer and reduce scaling.

The plurality of coils 30 are arranged in parallel along the height of the inlet riser 38.

The fluid enters the outermost heat exchange tube from the inlet of the inlet riser 38 through the pulsating tube, the heat exchange tube bundle vibrates under the flow of the fluid and the impact of the pulsating flow, and then the outermost heat exchange tube passes through the outlet riser of the outlet flow channel of the innermost heat exchange tube through the flow inside the heat exchange tube and finally flows out through the outlet riser.

Compared with the prior art, the inlet vertical pipe is connected with the inlet of the first heat exchange pipe through the pulse pipe, so that an independent pulse pipe is omitted, the inlet vertical pipe and the pulse pipe are combined into a whole, and the technical effects of simple structure, convenience in control and high heat exchange efficiency are realized. The pulsating flow generation can be controlled at any time by combining an external pulsating flow generation device.

Preferably, as shown in fig. 2, the pulse tube 37 is provided in plurality along the height direction of the inlet stand pipe 38. The pulse tube 37 has a diameter that becomes larger from the upper end to the lower end of the inlet stand pipe 38. Because found in experiment and practice, along with the continuous going on of heat transfer, the more toward lower extreme, the easier scale deposit of heat exchange tube at lower extreme more, consequently through the big some of pipe diameter distribution of this lower extreme for the flow of the pulsating flow of lower extreme distribution is also more, thereby makes the frequency of vibration also bigger, and the scale removal effect is also better, thereby leads to the whole obvious reinforcing of heat transfer effect.

Preferably, the pulse tube increases in diameter from upper to lower along the inlet riser 38. Because the experiment and practice find that along with the continuous proceeding of heat exchange, from top to bottom, the speed of scaling is not in direct proportion distribution, but the increasing amplitude of scaling is also increased, so the pipe diameter variation amplitude of the lower end is large, the flow increasing amplitude of pulsating flow distributed by the lower end is more, the frequency increasing amplitude of vibration is larger, the scaling effect is better, and the heat exchange effect is obviously enhanced on the whole.

Preferably, the coil 30 is provided in plurality along the height direction of the inlet stand pipe 38.

Preferably, at least one pulse tube bundle heat exchange assembly of the type described above with respect to FIGS. 3-5 is provided in the evaporator and/or condenser of the present application.

The heat exchanger below is referred to as an evaporator and/or a condenser.

Preferably, as shown in FIG. 7, a plurality of pulse tube bundle heat exchange assemblies 30-34 are arranged in the heat exchanger, wherein one is arranged in the center of the heat exchanger to form a central heat exchange assembly 30, and the other is distributed around the center of the heat exchanger to form peripheral heat exchange assemblies 31-34. Through the structural design, the fluid in the heat exchanger can fully achieve the vibration purpose, and the heat exchange effect is improved.

Preferably, the flow rate of the pulsating flow of the peripheral heat exchange assemblies 31 to 34 is smaller than the flow rate of the pulsating flow of the central heat exchanger 6. Through the design, the center reaches higher vibration frequency to form a central vibration source, so that the periphery is influenced, and better heat transfer enhancement and descaling effects are achieved.

Preferably, on the same horizontal heat exchange section, the fluid needs to achieve uniform vibration, and uneven heat exchange distribution is avoided. It is therefore desirable to distribute the magnitude of the pulsating flow in the different heat exchange assemblies appropriately. Experiments show that the distribution proportion of the flow of the pulsating flow of the central heat exchange assembly and the peripheral tube bundle heat exchange assembly is related to two key factors, wherein one of the two key factors is related to the distance between the peripheral heat exchange assembly and the center of the heat exchanger (namely the distance between the circle center of the peripheral heat exchange assembly and the circle center of the central heat exchange assembly) and the diameter of the heat exchanger. Therefore, the invention optimizes the optimal proportional distribution of the pulsating flow according to a large number of numerical simulations and experiments.

The heat exchanger is a circular section, the radius of the inner wall is R, the circle center of the central heat exchange assembly is arranged at the circle center of the circular section of the heat exchanger, the distance from the circle center of the peripheral heat exchange assembly to the circle center of the circular section of the heat exchanger is L, the circle centers of the adjacent peripheral heat exchange assemblies are respectively connected with the circle center of the circular section, the included angle formed by the two connecting lines is A, the pulsating flow of a single peripheral heat exchange assembly is M2, the pulsating flow of the central heat exchange assembly is M1, and the following requirements are met:

M1/M2=a*(R/L)²-b*(R/L)+c；

a, b, c are coefficients, where 0.0890< a <0.0896,0.4888< b <0.4892,2.8705< c < 2.8715;

preferably, 1.1< R/L < 2.3; preferably, 1.26< R/L < 2;

preferably, 2.2< M1/M2< 2.45. Preferably, 2.22< M1/M2< 2.4;

preferably, wherein 35 ° < a <80 °.

Preferably, the number of the four-side distribution is 4-5.

Preferably, R is from 2000 to 3000 mm, preferably 2500 mm; l is 1200 to 2400 mm, preferably 1800 mm; the diameter of the heat exchange tube is 12-20 mm, preferably 16 mm; the outermost diameter of the pulsating coil is 500-700 mm, preferably 600 mm. The diameter of the riser is 100-116 mm, preferably 108 mm, the height of the riser is 1.8-2.2 m, preferably 2 m, and the spacing between adjacent pulse tubes is 80-120 mm. Preferably around 100 mm.

Further preferably, a =0.0893, b =0.4890, c = 2.8709.

The pulse coil 30 is connected to the pulse tube 11 by a screw thread. The connected pulsating coil pipe can vibrate controllably under the induction of pulsating flow. The frequency and amplitude of the vibration is determined by the frequency of the pulsating flow in combination with the structural characteristics of the pulsating coil.

Fig. 3 is a schematic view of a pulsating coil arrangement. The pulsating tube heat exchange tubes 38 are connected by the counterweight blocks 25,40 to form a complete tube pass loop. Meanwhile, the heat exchange tube 38 is usually made of stainless steel, copper tube, or the like. Parameters such as the bending radius and the size of the used pipe and the heat exchange pipe 38 directly determine the vibration characteristic of the pulsating coil pipe, and the matching design is required according to the category of fused salt outside the pipe and the working temperature region.

Fig. 9 is a system diagram of a refrigerant operation process. A pulsation generating device 46 is provided on a line between the compressor and the condenser, or a pulsation generating device 42 is provided on a line between the expansion valve and the evaporator.

Preferably, as shown in fig. 11, a bypass line is provided in a main line between the compressor 1 and the condenser 2, the pulsation generating device 46 is provided in the bypass line, a main line valve 47 and a bypass valve 48 are provided in the main line and the bypass line between the compressor and the condenser in parallel with the bypass line, respectively, and whether or not the pulsating flow and the magnitude of the pulsating flow need to be generated are determined by opening and closing the main line valve 47 and the bypass valve 48.

The pulsation generating means is preferably a solenoid pump 46.

When it is found that the heat exchange capacity of the evaporator 2 is reduced or otherwise descaling is required, the bypass valve 48 is opened, the main valve 47 is closed, and water passes through the electromagnetic pump 46, creating a pulsating flow. And the bypass valve 48 is used for adjusting the generation time and generation intensity of the pulsating flow, so that the pulsating coil in the evaporator is induced and controlled to realize expected vibration, vibration-enhanced heat exchange of the tube bundle is realized, and the heat exchange efficiency is improved. The bypass valve 48 is configured to close and open the main valve for conditions not requiring pulsating flow oscillations.

The system further comprises a controller, wherein the electromagnetic pump 46, the main circuit valve 47 and the bypass valve 48 are in data connection with the controller, and the controller can control the frequency of the electromagnetic pump 46 and the opening, closing and amplitude of the main circuit valve 47 and the bypass valve 48.

Under normal operating conditions, the main circuit valve 47 is open, the bypass valve 48 is closed, and refrigerant enters the evaporator normally, impinging on the pulsating tube bundle vibration through the flow of fluid. When vibration descaling is needed or the heat exchange effect is improved, for example, the heat exchange efficiency is reduced, the controller controls the bypass valve to be opened, the main path valve to be closed, and the controller controls the electromagnetic pump to generate pulsating flow.

It is of course preferred that the heat exchange is always carried out by means of a pulsating flow.

Preferably, the sizes of the pulsating flow and the normal flow are automatically adjusted by controlling the sizes of the opening degrees of the bypass valve and the main valve.

The controller can control the magnitude of the pulsating flow as desired. For example, when the vibration noise of the heat exchange assembly is overlarge, the controller automatically controls the frequency or the flow rate of the pulsating flow to be reduced, and equipment damage is avoided.

When the vibration noise of the heat exchange assembly is too large, the opening degree of the bypass valve can be controlled to be reduced, and the opening degree of the main path valve is increased, so that the flow of pulsating flow and normal flow is adjusted, the whole heat exchange flow is kept unchanged, and the whole heat exchange efficiency is kept.

If the vibration noise is reduced to a certain degree, the opening degree of the bypass valve can be controlled to be increased, and the opening degree of the main path valve is reduced, so that the flow of pulsating flow and normal flow is adjusted, the whole heat exchange flow is kept unchanged, and the whole heat exchange efficiency is kept.

Preferably, the noise level is detected by an instrument, the instrument is in data connection with the controller, and the opening degree of the bypass valve and the opening degree of the main valve are automatically adjusted through the data detected by the controller.

Preferably, the adjustment can be performed manually.

By the above-mentioned intelligent control, pulsating flow generation in the evaporator and the frequency and speed of generation can be achieved.

Preferably, a bypass line is provided in the main line between the expansion valve 3 and the condenser 4, the pulsation generating device 42 is provided in the bypass line, and a bypass valve 44 and a main valve 43 are provided in both the main line and the bypass line between the expansion valve 3 and the condenser 4 in parallel with the bypass line, and whether or not a pulsating flow needs to be generated is determined by opening and closing the valves.

The pulsation generating means is preferably a solenoid pump 42.

When a drop in the heat transfer capacity of the condenser 4 is detected, or in other cases descaling is required, the bypass valve 44 is opened, the main valve 43 is closed, and the water passes through the electromagnetic pump 42, creating a pulsating flow. The bypass valve 44 is used for adjusting the generation time and generation intensity of the pulsating flow, so that the pulsating coil is induced and controlled to realize expected vibration, vibration-enhanced heat exchange of the tube bundle is realized, and the heat exchange efficiency is improved. The bypass valve 44 is configured for use in conditions where pulsating flow oscillations are not required. The main path valve is suitable for the working condition that pulsating flow vibration is not needed and can be closed, and the main path valve is opened.

The system further comprises a controller, wherein the electromagnetic pump 42, the main circuit valve 43 and the bypass valve 44 are in data connection with the controller, and the controller can control the frequency of the electromagnetic pump 42 and the opening, closing and amplitude of the main circuit valve 43 and the bypass valve 43.

Under normal operating conditions, main circuit valve 43 is open, bypass valve 44 is closed, and refrigerant enters the condenser normally, impinging on the pulsating tube bundle vibration through the flow of fluid. When vibration descaling is needed or the heat exchange effect is improved, for example, the heat exchange efficiency is reduced, the controller controls the bypass valve to be opened, the main path valve to be closed, and the controller controls the electromagnetic pump to generate pulsating flow.

It is of course preferred that the heat exchange is always carried out by means of a pulsating flow.

Preferably, the sizes of the pulsating flow and the normal flow entering the condenser are automatically adjusted by controlling the sizes of the opening degrees of the bypass valve and the main valve.

The controller can control the magnitude of the pulsating flow as desired. For example, when the vibration noise of the heat exchange assembly is overlarge, the controller automatically controls the frequency or the flow rate of the pulsating flow to be reduced, and equipment damage is avoided.

When the vibration noise of the heat exchange assembly is too large, the opening degree of the bypass valve 44 can be controlled to be reduced, and the opening degree of the main valve 43 is controlled to be increased, so that the flow of pulsating flow and normal flow is adjusted, the whole heat exchange flow is kept unchanged, and the whole heat exchange efficiency is kept.

If the vibration noise is reduced to a certain degree, the valve opening of the bypass valve 44 can be controlled to be increased, and the opening of the main valve 43 is reduced, so that the flow of pulsating flow and normal flow is adjusted, the whole heat exchange flow is kept unchanged, and the whole heat exchange efficiency is kept.

Preferably, the magnitude of the noise is detected by an instrument in data communication with the controller, and the opening of the bypass valve 44 and the main valve 43 is automatically adjusted by the data detected by the controller.

Preferably, the adjustment can be performed manually.

By the above-mentioned intelligent control, the pulsating flow generation of the condenser 4 and the frequency and speed of the generation can be realized.

Although the present invention has been described with reference to the preferred embodiments, it is not limited thereto. Various changes and modifications may be effected therein by one skilled in the art without departing from the spirit and scope of the invention as defined in the appended claims.

Claims (3)

1. A thermodynamic system for adjusting power change of a water pump is characterized by comprising a heat exchanger and an air cooler, wherein the air cooler is arranged on a working surface part; after exchanging heat with air in the air cooler to absorb the air, water enters the heat exchanger through a pipeline and is cooled in the heat exchanger, a temperature sensor is arranged on a working surface and is used for detecting the environment temperature of the underground working surface, a water pump is arranged between the heat exchanger and the air cooler, and when the detected temperature is higher than a certain temperature, the power of the water pump is increased more and more along with the continuous rise of the detected temperature;

when the detected temperature is lower than a certain temperature, the power of the water pump is continuously reduced with the continuous reduction of the detected temperature, and the power of the water pump is continuously reduced by a larger and larger amplitude.

2. A thermodynamic system as claimed in claim 1, wherein, when the sensed temperature is above 25 degrees celsius, the pump power increases by a greater and greater magnitude as the sensed temperature increases; when the detected temperature is lower than 5 ℃, the continuously reduced amplitude of the power of the water pump is larger and larger along with the continuous reduction of the detected temperature.

3. The utility model provides a heat exchanger, includes that elasticity tube bank subassembly includes coil pipe, import riser and export riser, the coil pipe is a plurality of, and every coil pipe includes convex many heat exchange tubes, and the tip of adjacent heat exchange tube communicates, makes many heat exchange tubes form the tandem structure to make the tip of heat exchange tube form the heat exchange tube free end, the import of first heat exchange tube is connected to the import riser, and the export of last heat exchange tube is connected to the export riser.

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