A plate heat exchanger with plug-in type forced flow optimization distribution

Abstract

The present invention relates to the field of plate heat exchange, and in particular to a plate heat exchanger with plug-in type forced flow optimization distribution, comprising two groups of side plates and six groups of corrugated plates, wherein the two groups of side plates and the six groups of corrugated plates are penetrated with four groups of through grooves, wherein the four groups of through grooves on one group of side plates are respectively detachably installed with a first pipe, a second pipe, a third pipe and a fourth pipe on the outward side, and the second pipe is located directly above the first pipe. The present invention can not only utilize the impact force when the refrigerant liquid and the cooling liquid are introduced to coordinate the rotation of multiple groups of different fan blades in the refrigeration zone and the cooling zone, and utilize the setting of the upper guide frame and the lower guide frame to promote the upper and lower halves of the refrigeration zone and the cooling zone to achieve balanced heat exchange, but also can accelerate the discharge of gaseous fluorine while prolonging the residence time of liquid fluorine in the refrigeration zone, thereby effectively improving the heat exchange effect and heat exchange efficiency of the entire device.

Description

Technical Field

[0001] The invention relates to the field of plate heat exchange, and in particular to a plate heat exchanger with plug-in type forced flow optimization distribution. Background Art

[0002] The plate heat exchanger is a high-efficiency heat exchanger composed of a series of metal sheets (i.e., heat exchange plates) with a certain corrugated shape. Thin rectangular channels are formed between various plates, and heat exchange is carried out through the plates. It is an ideal equipment for liquid-liquid and liquid-steam heat exchange. The types of plate heat exchangers are mainly frame type (detachable type) and brazed type. Among them, the detachable plate heat exchanger is composed of many stamped corrugated thin plates at a certain interval, sealed by gaskets on all sides, and overlapped and compressed with frames and compression spirals. The four corner holes of the plates and gaskets form the distribution pipes and collection pipes of the fluid, and at the same time, the cold and hot fluids are reasonably separated, so that they flow in the flow channels on both sides of each plate respectively, and heat exchange is carried out through the plates.

[0003] Most existing plate heat exchangers directly introduce the refrigerant and the coolant into the device, and then enter adjacent and isolated areas for heat exchange, and then discharge them after the heat exchange is completed. In this design, the flow directions of the refrigerant and the coolant are usually opposite, that is, one flows from bottom to top and the other flows from top to bottom. This countercurrent arrangement is designed to maximize the heat exchange efficiency. However, in actual operation, there is a problem of inconsistent flow rate. Specifically, the flow rate of the refrigerant and the coolant is relatively fast when they first enter the heat exchange area, but when they are about to flow out, that is, when they are close to the outlet, the flow rate will gradually slow down due to the consumption of kinetic energy. This inconsistency in flow rate will lead to uneven heat exchange process. Specifically, the faster-flowing fluid may not be fully discharged before heat exchange with the slower-flowing fluid, resulting in uneven heat exchange in the entire plate heat exchanger, thereby reducing the heat exchange effect and poor practicality. Summary of the invention

[0004] The purpose of the present invention is to solve the problem that most existing plate heat exchangers have inconsistent flow rates during actual operation, which easily leads to uneven heat exchange and thus reduces the heat exchange effect. A plate heat exchanger with plug-in type forced flow optimization distribution is proposed.

[0005] In order to achieve the above-mentioned purpose, the present invention adopts the following technical scheme: a plate heat exchanger with plug-in type forced flow optimization distribution, comprising two groups of side plates and six groups of corrugated plates, the two groups of side plates and the six groups of corrugated plates are penetrated with four groups of through grooves, the four groups of through grooves on one group of side plates are respectively detachably installed with a first pipe, a second pipe, a third pipe and a fourth pipe on the outward side, the second pipe is located directly above the first pipe, and the third pipe is located directly above the fourth pipe, and the four groups of through grooves on the other group of side plates are detachably installed with sealing plugs on the outward side, and also include:

[0006] A fixing mechanism, which is arranged on the two groups of side plates and the six groups of corrugated plates and is used to press and fix the two groups of side plates and the six groups of corrugated plates;

[0007] Seven groups of sealing gaskets, wherein five groups of the sealing gaskets are respectively inserted between two adjacent groups of corrugated plates among the six groups of corrugated plates, and the other two groups of the sealing gaskets are respectively inserted between two groups of side plates and two adjacent groups of corrugated plates thereto, and two adjacent groups of sealing gaskets among the seven groups of the sealing gaskets are arranged in opposite directions to each other, and the areas where the two adjacent groups of the sealing gaskets are located are respectively a cooling zone and a refrigeration zone, and the sealing gaskets are arranged in a trapezoidal shape inclined at 90 degrees, and isolation rings are installed on the edges of one side of the top and bottom ends of the sealing gaskets that are inclined downward, the first connecting pipe and the second connecting pipe correspond to the positions of the two groups of isolation rings on the sealing gasket in the cooling zone, and the third connecting pipe and the fourth connecting pipe correspond to the positions of the two groups of isolation rings on the sealing gasket in the refrigeration zone;

[0008] A liquid separation mechanism, the liquid separation mechanism is arranged on the first connecting pipe and a group of sealing plugs corresponding thereto, and is used to make the flow rate of the refrigerant entering the refrigeration zone the same;

[0009] The first auxiliary mechanism and the second auxiliary mechanism are both arranged in the seven groups of sealing gaskets. The first auxiliary mechanism is used to reduce the flow rate of the refrigerant liquid entering the refrigeration zone for the first time and to give kinetic energy to the refrigerant liquid that is about to flow out of the refrigeration zone. The second auxiliary mechanism is used to give kinetic energy to the refrigerant liquid that is about to flow out of the refrigeration zone and to reduce the flow rate of the refrigerant liquid entering the refrigeration zone for the first time.

[0010] Preferably, the area where the sealing gasket is located near the side plate is the cooling zone, and there are seven groups of cooling zones and refrigeration zones in total, four groups of cooling zones, and three groups of refrigeration zones. A group of sealing sheets is detachably installed at the installation location of the first connecting pipe and the side plate, and another group of sealing sheets is detachably installed at the installation location of the sealing plug opposite to the first connecting pipe and the side plate.

[0011] Preferably, the fixing mechanism includes four groups of fixing columns, which are respectively inserted through four groups of corners on two groups of side plates and six groups of corrugated plates, and fixing nuts are detachably installed at both ends of the four groups of fixing columns. The liquid distributing mechanism includes a distribution pipe, the end of the first connecting pipe facing the side plate is closed, one end of the distribution pipe is inserted through the end of the first connecting pipe facing the side plate, and the other end of the distribution pipe passes through the through grooves corresponding to the position of the first connecting pipe on the two groups of side plates and six groups of corrugated plates, and is detachably installed on the inward end of the sealing plug corresponding to the first connecting pipe, the bottom end of the distribution pipe is fixedly connected to a connecting block, three groups of spray valves are fixedly installed on the connecting block, the top ends of the three groups of spray valves are all installed with connecting pipes, and the three groups of spray valves are all connected to the inside of the distribution pipe through the connecting pipe, the bottom ends of the three groups of spray valves are all provided with streamlined nozzles, and the positions of the three groups of spray valves respectively correspond to the positions of the three groups of refrigeration zones.

[0012] Preferably, the first auxiliary mechanism includes a flow reducing component and three groups of lower guide frames, the three groups of lower guide frames are respectively inserted between two groups of corrugated plates in the three groups of refrigeration zones, the positions of the three groups of lower guide frames all correspond to the positions of the first connecting pipes, and the inner walls of the three groups of lower guide frames facing the isolation ring are penetrated by liquid outlets, the liquid outlets are located close to the top of the lower guide frames, the flow reducing component is arranged in the three groups of refrigeration zones, and is used to interfere with the refrigerant that has just entered the refrigeration zone, and the four groups of cold-carrying zones are provided with energy-enhancing components, which are used to give kinetic energy to the cold-carrying liquid that is about to flow out of the cold-carrying zone.

[0013] Preferably, the flow reduction component includes two groups of first rotating shafts and two groups of connecting side shafts, the two groups of first rotating shafts are located between the two groups of connecting side shafts, the outward ends of the two groups of connecting side shafts are respectively rotatably connected to the inner side walls of the two groups of side plates, and the inward ends of the two groups of connecting side shafts penetrate a group of corrugated plates and extend toward a group of refrigeration zones respectively, one group of the first rotating shafts penetrates and is rotatably connected to two groups of corrugated plates among the four groups of corrugated plates located in the middle, and the other group of the first rotating shafts penetrates and is rotatably connected to the other two groups of corrugated plates among the four groups of corrugated plates located in the middle, the two groups of the first rotating shafts are symmetrical to each other, and the opposite ends of the two groups of the first rotating shafts are jointly located in a group of refrigeration zones, and the non-opposite ends of the two groups of the first rotating shafts are respectively connected to the two groups The inward end of the connecting shaft is located in the same group of refrigeration zones, and multiple groups of first fan blades are fixedly connected to the outer walls of one end of the two groups of connecting shafts located in the refrigeration zone and both ends of the two groups of first rotating shafts located in the refrigeration zone. The multiple groups of first fan blades in the three groups of refrigeration zones are respectively located in the three groups of lower guide frames, and the positions of the multiple groups of first fan blades in the three groups of refrigeration zones correspond to the positions of the liquid outlets in the three groups of lower guide frames. The multiple groups of first fan blades are all inclined, and diversion grooves are penetrated by the side walls of the three groups of lower guide frames near the positions of the multiple groups of first fan blades. The opposite ends of the two groups of first rotating shafts are respectively located on both sides of one group of diversion grooves, and the non-opposite ends of the two groups of first rotating shafts and the inward ends of the two groups of connecting shafts are respectively located on both sides of the other two groups of diversion grooves.

[0014] Preferably, the energy boosting component includes four groups of lower guide plates, wherein two groups of the lower guide plates are respectively inserted between two groups of corrugated plates in two groups of refrigeration zones, and the other two groups of the lower guide plates are respectively inserted between one group of side plates and one group of corrugated plates in the other two groups of refrigeration zones, and the heights of the four groups of lower guide plates are between the third connecting pipe and the fourth connecting pipe, and multiple groups of fourth fan blades are installed at the middle position of the outer walls of the two groups of the first rotating shafts and the two groups of connecting side shafts, and the multiple groups of fourth fan blades on the outer walls of the two groups of the first rotating shafts and the two groups of connecting side shafts are respectively located in the four groups of cooling zones, and the multiple groups of fourth fan blades are all V-shaped structures, and the multiple groups of fourth fan blades located in the cooling zone are close to the isolation ring position on the sealing gasket in the cooling zone, and the tips of the above-mentioned multiple groups of fourth fan blades are facing the direction of the lower guide plate, one end of the lower guide plate is in contact with the inner wall of one side of the sealing gasket, and the other end of the lower guide plate is close to the multiple groups of fourth fan blades.

[0015] Preferably, the second auxiliary mechanism includes three groups of upper guide frames, the three groups of upper guide frames are respectively inserted between two groups of corrugated plates of three groups of refrigeration zones, and the three groups of upper guide frames are respectively located directly above the three groups of lower guide frames, the positions of the three groups of upper guide frames all correspond to the positions of the second connecting pipes, and the inner walls of the three groups of upper guide frames facing the isolation ring are penetrated by a liquid inlet, the liquid inlet is located close to the bottom of the upper guide frame, and a baffle is fixedly installed at the middle position of the inner wall of the three groups of upper guide frames, and the width of the baffle is smaller than the width of the upper guide frame, and the three groups of refrigeration zones and the four groups of cooling zones are commonly provided with a deceleration and energy-enhancing component, which is used to give kinetic energy to the cooling liquid that is about to flow out of the refrigeration zone and interfere with the cooling liquid that has just entered the cooling zone.

[0016] Preferably, the deceleration and energy-boosting assembly comprises six groups of adapter boxes, two groups of edge shells, three groups of second rotating shafts and four groups of third rotating shafts. The two groups of edge shells penetrate and are detachably mounted on the two groups of side plates, and the two groups of edge shells correspond to the positions of the six groups of adapter boxes. The six groups of adapter boxes respectively penetrate and are detachably mounted on the six groups of corrugated plates. The three groups of second rotating shafts are respectively located in the three groups of refrigeration zones, and the two ends of the three groups of second rotating shafts respectively penetrate the outer side walls of two adjacent groups of adapter boxes in the six groups of adapter boxes and are rotatably connected to the corresponding adapter boxes. Each group of the second rotating shafts is respectively located between every two groups of third rotating shafts, and the four groups of third rotating shafts are located in the four groups of cooling zones, wherein the two ends of the two groups of third rotating shafts respectively penetrate the outer side walls of two adjacent groups of adapter boxes in the middle four groups of adapter boxes and are rotatably connected to the corresponding adapter boxes, and the outward ends of the other two groups of third rotating shafts are rotatably connected to the two groups of edge shells respectively, and the inward ends of the two groups of third rotating shafts respectively penetrate the outermost The outer walls of the two groups of adapter boxes are rotatably connected with the corresponding adapter boxes, the three groups of second rotating shafts are all located above the four groups of third rotating shafts, and multiple groups of second fan blades are fixedly connected to the outer walls of the three groups of second rotating shafts, the multiple groups of second fan blades are all V-shaped structures, and the multiple groups of second fan blades are all curved, the multiple groups of second fan blades on the three groups of second rotating shafts are respectively located in the three groups of upper guide frames, and the positions of the multiple groups of second fan blades on the three groups of second rotating shafts correspond to the positions of the liquid inlets in the three groups of upper guide frames, the multiple groups of second fan blades are located below the baffle on the upper guide frame, the four groups of third rotating shafts are all fixedly connected to the outer walls of the multiple groups of third fan blades, the multiple groups of third fans are all straightly set, the multiple groups of third fan blades in each group of the cooling zone are all located directly above the multiple groups of fourth fan blades in each group of the cooling zone, and large gears and small gears are respectively installed on the outer walls of the third rotating shaft and the second rotating shaft parts located in the six groups of the adapter boxes, and the large gears and small gears are meshed with each other.

[0017] Preferably, each of the four groups of cooling zones is provided with a group of upper guide plates and a group of middle guide plates, two groups of the four groups of upper guide plates and two groups of the four groups of middle guide plates are respectively inserted between the two groups of corrugated plates in the two refrigeration zones, the other two groups of the upper guide plates and the other two groups of middle guide plates are respectively inserted between a group of side plates and a group of corrugated plates in the other two refrigeration zones, the upper guide plate is located above the lower guide plate, the middle guide plate is located between the upper guide plate and the lower guide plate, one end of the upper guide plate is in contact with the inner wall of one side of the sealing gasket, and the other end of the upper guide plate is close to multiple groups of third fan blades, one end of the middle guide plate is in contact with the inner wall of the other side of the sealing gasket, and the middle guide plate is located between multiple groups of third fan blades and multiple groups of fourth fan blades.

[0018] Preferably, it also includes three groups of stabilizing mechanisms, which are respectively arranged in three groups of refrigeration zones, and the stabilizing mechanisms include two groups of fixing sleeves, the two groups of fixing sleeves are respectively fixedly installed at the middle position of the opposite side of the two groups of corrugated plates in the refrigeration zone, and both ends of the two groups of fixing sleeves are in contact with the inner wall of the sealing gasket in the refrigeration zone, one group of the fixing sleeves is located above the other group of fixing sleeves, and two groups of sliding grooves are respectively opened in the fixing sleeves near the two end edges, and sliders are sealingly and slidably connected in the two groups of sliding grooves, and movable rods are installed on the two groups of sliding grooves, and the ends of the two groups of movable rods away from the sliders penetrate the inner wall of the sliding grooves and are fixedly connected with movable blocks together, and the part of the movable rod located in the sliding groove is provided with a spring, one end of the spring is fixedly connected to the slider, and the other end of the spring is fixedly connected to the inner wall of the sliding groove, the two groups of movable blocks are arranged at an oblique angle toward the side of the two groups of fixing sleeves, and there are gaps between the two groups of corrugated plates and the sides of the two groups of movable blocks away from the two groups of fixing sleeves.

[0019] Compared with the prior art, the advantages of the present invention are:

[0020] 1. The present invention, through the mutual cooperation of the first auxiliary mechanism and the second auxiliary mechanism, can not only utilize the impact force when the refrigerant liquid and the coolant are introduced to coordinate the rotation of multiple groups of different fan blades in the refrigeration zone and the coolant zone, and utilize the setting of the upper guide frame and the lower guide frame to promote the upper and lower parts of the refrigeration zone and the coolant zone to achieve balanced heat exchange (that is, relatively uniform heat exchange), but also can prolong the residence time of liquid fluorine (refrigerant) in the refrigeration zone while accelerating the discharge of gaseous fluorine, thereby effectively improving the heat exchange effect and heat exchange efficiency of the entire device.

[0021] 2. The present invention can realize accurate distribution of the flow rate of refrigerant liquid entering the refrigeration zone through the setting of the liquid distribution mechanism. When the refrigerant liquid enters the first connecting pipe, the distribution pipe and the three groups of liquid spray valves at the bottom end thereof can be used to evenly distribute the refrigerant liquid to three different refrigeration zones, thereby effectively ensuring that the flow rate of refrigerant liquid entering the three groups of refrigeration zones is the same, thereby ensuring that the heat exchange conditions in each area are relatively consistent, avoiding the phenomenon of uneven local heat exchange caused by uneven flow rate, and effectively improving the heat exchange effect.

[0022] 3. The present invention, through the arrangement of a stabilizing mechanism in the refrigeration zone, can utilize the pressure exerted on the two groups of movable blocks by the flow of refrigerant in the refrigeration zone to compress the spring, and apply a pulling force to the two groups of fixed sleeves under the elastic force of the compressed spring, thereby indirectly applying a force in the opposite direction to the corrugated plates, thereby ensuring that the two groups of corrugated plates in the refrigeration zone can effectively prevent the leakage of the refrigerant even when facing a large internal impact (i.e., the impact of the refrigerant), thereby effectively ensuring the smooth progress of the heat exchange process.

[0023] 4. The present invention can guide the cooling liquid in the cooling zone through the mutual cooperation of the upper guide plate, the middle guide plate and the lower guide plate in the cooling zone, and can also use the setting of the middle guide plate to increase the residence time of the cooling liquid in the cooling zone to enable better heat exchange, thereby further ensuring the smooth progress of the heat exchange process and further improving the heat exchange effect. BRIEF DESCRIPTION OF THE DRAWINGS

[0024] Figure 1 This is a schematic diagram of the overall structure of a plate heat exchanger with plug-in type forced flow optimization distribution proposed by the present invention;

[0025] Figure 2 An exploded view of the corrugated plate and sealing sheet of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0026] Figure 3 A half-section diagram of the corrugated plate and sealing sheet of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0027] Figure 4 This is a schematic diagram of the structure of a plate heat exchanger distribution pipe and a liquid injection valve part for a plug-in type forced flow optimization distribution proposed by the present invention;

[0028] Figure 5 This is a structural schematic diagram of the upper guide frame and the lower guide frame of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0029] Figure 6 This is a schematic structural diagram of the first fan section of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0030] Figure 7 This is a schematic structural diagram of the first rotating shaft and the connecting shaft part of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0031] Figure 8 A half-section diagram of a fixed sleeve and a movable block of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0032] Fig. 9 This is a schematic structural diagram of the second fan section of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0033] Fig.10 A half-section diagram of a plate heat exchanger adapter box portion for a plug-in type forced flow optimization distribution proposed by the present invention;

[0034] Fig.11 An exploded view of a plate heat exchanger adapter box and an edge shell portion for a plug-in type forced flow optimization distribution proposed by the present invention;

[0035] Fig.12 This is a schematic structural diagram of an upper guide plate, a middle guide plate and a lower guide plate of a plate heat exchanger with a plug-in type forced flow optimization distribution proposed by the present invention;

[0036] Fig.13 for Fig.12 The enlarged view of point A in the middle;

[0037] Fig.14 for Fig.12 Enlarged view of point B in the middle.

[0038] In the figure: 1, side plate; 10, corrugated plate; 11, fixing column; 12, fixing nut; 13, adapter box; 130, edge shell; 131, small gear; 132, large gear; 14, sealing sheet; 2, first connecting pipe; 21, second connecting pipe; 22, third connecting pipe; 23, fourth connecting pipe; 24, sealing plug; 25, distribution pipe; 26, spray valve; 261, streamlined nozzle; 27, connecting block; 3, sealing pad; 31, upper guide plate; 32, middle guide plate; 33. Lower guide plate; 4. Lower guide frame; 41. Diverter slot; 411. Liquid outlet; 42. First rotating shaft; 421. Connecting shaft; 43. First blade; 44. Fixed sleeve; 441. Movable block; 442. Movable rod; 443. Spring; 45. Upper guide frame; 451. Baffle; 452. Liquid inlet; 46. Second rotating shaft; 461. Second blade; 5. Third rotating shaft; 51. Third blade; 52. Fourth blade; 6. Cooling zone; 7. Refrigeration zone. DETAILED DESCRIPTION

[0039] The technical solutions in the embodiments of the present invention will be described clearly and completely below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all the embodiments.

[0040] Reference Figures 1 to 3 A plate heat exchanger with plug-in type forced flow optimization distribution includes two sets of side plates 1, six sets of corrugated plates 10 and seven sets of sealing gaskets 3. The number of corrugated plates 10 can be flexibly selected and installed according to actual needs. The above six sets of corrugated plates 10 are only used for description in conjunction with the drawings and do not represent the fixed number actually used. The two sets of side plates 1 and the six sets of corrugated plates 10 are all penetrated by four sets of through grooves. The four sets of through grooves on one set of side plates 1 are respectively detachably installed with a first pipe 2, a second pipe 21, The third pipe 22 and the fourth pipe 23, the second pipe 21 is located directly above the first pipe 2, the third pipe 22 is located directly above the fourth pipe 23, the four groups of through grooves on the other side plate 1 are all removably installed with sealing plugs 24 on the outward side, the six groups of corrugated plates 10 are all located between the two groups of side plates 1, and the two groups of side plates 1 and the six groups of corrugated plates 10 are jointly provided with a fixing mechanism for pressing and fixing the two groups of side plates 1 and the six groups of corrugated plates 10, the fixing mechanism includes four groups of fixing columns 11, the four groups of fixing columns 11 The four groups of corners are respectively inserted through the two groups of side plates 1 and the six groups of corrugated plates 10, and the two ends of the four groups of fixing columns 11 are detachably installed with fixing nuts 12, wherein five groups of sealing gaskets 3 are respectively inserted between two adjacent groups of corrugated plates 10 in the six groups of corrugated plates 10, and the other two groups of sealing gaskets 3 are respectively inserted between the two groups of side plates 1 and the two adjacent groups of corrugated plates 10, and the adjacent two groups of sealing gaskets 3 in the seven groups of sealing gaskets 3 are arranged in opposite directions to each other, and the areas where the adjacent two groups of sealing gaskets 3 are located are respectively the load Cold zone 6 and refrigeration zone 7, the area where the sealing gasket 3 near the side plate 1 is located is the cold zone 6, and there are seven groups in total in the cold zone 6 and the refrigeration zone 7, there are four groups in the cold zone 6, and there are three groups in the refrigeration zone 7 (because there are seven groups of sealing gaskets 3, and the areas where two adjacent groups of sealing gaskets 3 are located are the cold zone 6 and the refrigeration zone 7 respectively, there are seven groups in total in the cold zone 6 and the refrigeration zone 7, and at the same time, because the area where the two groups of sealing gaskets 3 near the two groups of side plates 1 are located is the cold zone 6, there are four groups in the cold zone 6 and there are three groups in the refrigeration zone 7).

[0041] Reference Figures 2 to 5The sealing gasket 3 is set in a trapezoidal shape inclined at 90 degrees, and isolation rings are installed on the edges of the top and bottom of the sealing gasket 3 that are inclined downward. The shapes of the multiple groups of sealing gaskets 3 are set as the conventional settings of the plate heat exchanger, so that the refrigerant liquid and the cooling liquid can be respectively passed into the adjacent and mutually isolated areas formed by the multiple groups of corrugated plates 10 along different channels, and the two liquids will not come into direct contact. The first connecting pipe 2 and the second connecting pipe 21 correspond to the positions of the two groups of isolation rings on the sealing gasket 3 in the cooling area 6, and the third connecting pipe 22 and the fourth connecting pipe 23 correspond to the positions of the two groups of isolation rings on the sealing gasket 3 in the refrigeration area 7. A group of sealing sheets 14 are detachably installed at the installation place of the first connecting pipe 2 and the side plate 1, and another group of sealing sheets 14 are detachably installed at the installation place of a group of sealing plugs 24 opposite to the first connecting pipe 2 and the side plate 1. The sealing sheets 14 are used to avoid liquid leakage at the above-mentioned installation places, thereby ensuring the smooth progress of the entire heat exchange process.

[0042] Reference Figures 1 to 5 The first connecting pipe 2 and a corresponding group of sealing plugs 24 are jointly provided with a liquid separation mechanism for making the pressure and flow rate of the refrigerant (liquid fluorine) entering the refrigeration zone 7 the same. The liquid separation mechanism includes a distribution pipe 25. The end of the first connecting pipe 2 facing the side plate 1 is closed. One end of the distribution pipe 25 is inserted through the end of the first connecting pipe 2 facing the side plate 1, and the other end of the distribution pipe 25 passes through the through grooves corresponding to the position of the first connecting pipe 2 on the two groups of side plates 1 and the six groups of corrugated plates 10, and is detachably installed on the inward end of the sealing plug 24 corresponding to the first connecting pipe 2. A connecting block 27 is fixedly connected to the bottom end of the distribution pipe 25. Three groups of liquid spray valves 26 are fixedly installed on the connecting block 27. The top ends of the three groups of liquid spray valves 26 are all provided with connecting pipes, and the three groups of liquid spray valves 26 are all connected to the inside of the distribution pipe 25 through the connecting pipes. The bottom ends of the three groups of liquid spray valves 26 are all provided with streamlined nozzles 261, and the positions of the three groups of liquid spray valves 26 correspond to the positions of the three groups of refrigeration zones 7 respectively.

[0043] Reference Figures 2 to 14The seven groups of sealing pads 3 are commonly provided with a first auxiliary mechanism for decelerating the refrigerant initially entering the refrigeration zone 7 and giving kinetic energy to the refrigerant that is about to flow out of the cooling zone 6. The first auxiliary mechanism includes a flow reduction component and three groups of lower guide frames 4. The three groups of lower guide frames 4 are respectively inserted between the two groups of corrugated plates 10 of the three groups of refrigeration zones 7. The positions of the three groups of lower guide frames 4 correspond to the positions of the first connecting pipes 2. The inner side walls of the three groups of lower guide frames 4 facing the isolation ring are penetrated with a liquid outlet 411. The position of the liquid outlet 411 is close to the top of the lower guide frame 4. The flow reduction component is arranged on the three groups of lower guide frames 4. The flow reducing assembly comprises two groups of first rotating shafts 42 and two groups of connecting side shafts 421. The two groups of first rotating shafts 42 are located between the two groups of connecting side shafts 421. The outward ends of the two groups of connecting side shafts 421 are respectively rotatably connected with the inner side walls of the two groups of side plates 1. The inward ends of the two groups of connecting side shafts 421 penetrate a group of corrugated plates 10 and extend into a group of refrigerating zones 7 respectively. One group of first rotating shafts 42 penetrates and is rotatably connected to two groups of corrugated plates 10 among the four groups of corrugated plates 10 located in the middle. The other group of first rotating shafts 42 penetrates and is rotatably connected to the inner side walls of the two groups of side plates 1. The two first rotating shafts 42 are symmetrical to each other, and the opposite ends of the two first rotating shafts 42 are located in one refrigeration zone 7. The opposite ends of the two first rotating shafts 42 are located in the same refrigeration zone 7 as the inward ends of the two connecting side shafts 421 (that is, the opposite ends of the two first rotating shafts 42 are located in the other two refrigeration zones 7). Multiple sets of first blades are fixedly connected to the outer walls of the ends of the two connecting side shafts 421 located in the refrigeration zone 7 and the two ends of the two first rotating shafts 42 located in the refrigeration zone 7. 43, the multiple groups of first fan blades 43 in the three refrigeration zones 7 are respectively located in the three groups of lower guide frames 4, and the positions of the multiple groups of first fan blades 43 in the three refrigeration zones 7 correspond to the positions of the liquid outlets 411 in the three groups of lower guide frames 4, the multiple groups of first fan blades 43 are all inclined, and the side walls of the three groups of lower guide frames 4 are penetrated by diversion grooves 41 near the positions of the multiple groups of first fan blades 43, the opposite ends of the two groups of first rotating shafts 42 are respectively located on both sides of one group of diversion grooves 41, and the non-opposite ends of the two groups of first rotating shafts 42 and the inward ends of the two groups of connecting shafts 421 are respectively located on both sides of the other two groups of diversion grooves 41.

[0044] Reference Figure 2 as well as Figures 7 to 14, energy-enhancing components are provided in the four groups of cooling zones 6 for giving kinetic energy to the cooling liquid that is about to flow out of the cooling zone 6, and the energy-enhancing components include four groups of lower guide plates 33, two of which are respectively inserted between the two groups of corrugated plates 10 of the two groups of refrigeration zones 7, and the other two groups of lower guide plates 33 are respectively inserted between a group of side plates 1 and a group of corrugated plates 10 of the other two groups of refrigeration zones 7, and the heights of the four groups of lower guide plates 33 are all between the third pipe 22 and the fourth pipe 23, and multiple groups of fourth blades 52 are installed at the middle position of the outer wall of the two groups of first rotating shafts 42 and the two groups of connecting side shafts 421. The multiple groups of fourth fan blades 52 on the outer walls of the rotating shaft 42 and the two groups of connecting shafts 421 are respectively located in the four groups of cooling zones 6. The multiple groups of fourth fan blades 52 all have a V-shaped structure. The multiple groups of fourth fan blades 52 located in the cooling zone 6 are located close to the isolation ring position on the sealing gasket 3 in the cooling zone 6, and the tips of the multiple groups of fourth fan blades 52 are facing the lower guide plate 33. One end of the lower guide plate 33 is in contact with the inner wall of one side of the sealing gasket 3, and the other end of the lower guide plate 33 is close to the multiple groups of fourth fan blades 52. The lower guide plate 33 can guide the cooling liquid so that the cooling liquid can better act on the fourth fan blades 52.

[0045] Reference Figures 2 to 13The seven groups of sealing pads 3 are commonly provided with a second auxiliary mechanism for giving kinetic energy to the coolant that is about to flow out of the refrigeration zone 7 and for decelerating the coolant that is just entering the refrigeration zone 6. The second auxiliary mechanism includes three groups of upper guide frames 45, which are respectively inserted between the two groups of corrugated plates 10 of the three groups of refrigeration zones 7, and the three groups of upper guide frames 45 are respectively located directly above the three groups of lower guide frames 4, and the positions of the three groups of upper guide frames 45 correspond to the positions of the second connecting pipes 21, and the three groups of upper guide frames 45 face the isolation ring. The inner wall of the upper guide frame 45 is provided with a liquid inlet 452, and the liquid inlet 452 is located near the bottom of the upper guide frame 45. A baffle 451 is fixedly installed at the middle position of the inner wall of the three groups of upper guide frames 45. The width of the baffle 451 is smaller than the width of the upper guide frame 45. The three groups of refrigeration zones 7 and the four groups of cooling zones 6 are provided with a deceleration and energy-enhancing component for giving kinetic energy to the cooling liquid that is about to flow out of the refrigeration zone 7 and reducing the speed of the cooling liquid that initially enters the cooling zone 6. The deceleration and energy-enhancing component includes six groups of adapter boxes 13, two groups of edge shells 130, three groups of second rotating shafts 46 and four groups of third rotating shafts 5, two groups of edge shells 130 penetrate and are detachably mounted on two groups of side plates 1, and the two groups of edge shells 130 correspond to the positions of six groups of adapter boxes 13, and the six groups of adapter boxes 13 penetrate and are detachably mounted on six groups of corrugated plates 10, respectively, and the three groups of second rotating shafts 46 are respectively located in three groups of refrigeration zones 7, and the two ends of the three groups of second rotating shafts 46 respectively penetrate the outer side walls of two adjacent groups of adapter boxes 13 in the six groups of adapter boxes 13, and are rotatably connected with the corresponding adapter boxes 13, and each group of second The rotating shaft 46 is respectively located between every two groups of third rotating shafts 5, and the four groups of third rotating shafts 5 are located in four groups of cold-carrying areas 6, wherein the two ends of the third rotating shafts 5 respectively penetrate the outer side walls of two adjacent groups of adapter boxes 13 among the four groups of adapter boxes 13 located in the middle, and are rotatably connected to the corresponding adapter boxes 13, and the outward ends of the other two groups of third rotating shafts 5 are respectively rotatably connected to the two groups of edge shells 130, and the inward ends of the two groups of third rotating shafts 5 respectively penetrate the outer side walls of the two outermost groups of adapter boxes 13, and are rotatably connected to the corresponding adapter boxes 13.

[0046] Reference Figure 2 as well as Figures 7 to 13The three groups of second rotating shafts 46 are all located above the four groups of third rotating shafts 5, and multiple groups of second fan blades 461 are fixedly connected to the outer walls of the three groups of second rotating shafts 46, and the multiple groups of second fan blades 461 are all V-shaped structures, and the multiple groups of second fan blades 461 are all arranged in a curved shape. The multiple groups of second fan blades 461 on the three groups of second rotating shafts 46 are respectively located in the three groups of upper guide frames 45, and the positions of the multiple groups of second fan blades 461 on the three groups of second rotating shafts 46 correspond to the positions of the liquid inlets 452 in the three groups of upper guide frames 45. The fan blades 461 are located below the spoiler 451 on the upper guide frame 45, and multiple groups of third fan blades 51 are fixedly connected to the outer walls of the four groups of third rotating shafts 5. The multiple groups of third fans are all arranged straightly. The multiple groups of third fan blades 51 in each group of cooling zones 6 are located directly above the multiple groups of fourth fan blades 52 in each group of cooling zones 6. The large gear 132 and the small gear 131 are respectively installed on the outer walls of the third rotating shaft 5 and the second rotating shaft 46 located in the six groups of adapter boxes 13, and the large gear 132 and the small gear 131 are meshed with each other.

[0047] Reference Figure 2 and Fig.12 , each of the four groups of cooling zones 6 is provided with a group of upper guide plates 31 and a group of middle guide plates 32, two groups of upper guide plates 31 among the four groups of upper guide plates 31 and two groups of middle guide plates 32 among the four groups of middle guide plates 32 are respectively inserted between the two groups of corrugated plates 10 of the two groups of refrigeration zones 7, and the other two groups of upper guide plates 31 and the other two groups of middle guide plates 32 are respectively inserted between a group of side plates 1 and a group of corrugated plates 10 of the other two groups of refrigeration zones 7, the upper guide plates 31 are located above the lower guide plates 33, and the middle guide plates 32 are located between the upper guide plates 31 and the lower guide plates 33 One end of the upper guide plate 31 is in contact with the inner wall of one side of the sealing gasket 3, and the other end of the upper guide plate 31 is close to the multiple groups of third fan blades 51, one end of the middle guide plate 32 is in contact with the inner wall of the other side of the sealing gasket 3, and the middle guide plate 32 is located between the multiple groups of third fan blades 51 and the multiple groups of fourth fan blades 52. The upper guide plate 31 can guide the cooling liquid so that the cooling liquid can better act on the third fan blades 51, and the middle guide plate 32 can increase the residence time of the cooling liquid in the cooling zone 6 while guiding the cooling liquid to enable it to better exchange heat.

[0048] Reference Figure 2 , Figure 5 and Figure 8The three groups of refrigeration zones 7 are all provided with a stabilizing mechanism for making the connection between the six groups of corrugated plates 10 more stable. The stabilizing mechanism includes two groups of fixing sleeves 44, which are respectively fixedly mounted at the middle position of the two groups of corrugated plates 10 on the opposite sides of the refrigeration zone 7, and both ends of the two groups of fixing sleeves 44 are in contact with the inner wall of the sealing gasket 3 in the refrigeration zone 7, one group of fixing sleeves 44 is located above the other group of fixing sleeves 44, and two groups of sliding grooves are respectively opened near the edges of both ends in the fixing sleeves 44, and sliders are sealed and slidably connected in the two groups of sliding grooves. Movable rods 442 are installed on both sets of sliders. The ends of the two sets of movable rods 442 away from the sliders penetrate the inner wall of the slide groove and are fixedly connected with a movable block 441. The part of the movable rod 442 located in the slide groove is provided with a spring 443. One end of the spring 443 is fixedly connected to the slider, and the other end of the spring 443 is fixedly connected to the inner wall of the slide groove. The two sets of movable blocks 441 are arranged at an oblique angle toward one side of the two sets of fixed sleeves 44, and there is a gap between the two sets of corrugated plates 10 and the two sets of fixed sleeves 44.

[0049] In the present invention, when heat exchange is required, the refrigerant (liquid fluorine) and the cooling liquid (50% ethylene glycol solution) are respectively introduced into the entire device through the first connecting pipe 2 and the third connecting pipe 22. Since the first connecting pipe 2 and the second connecting pipe 21 correspond to the positions of the two sets of isolation rings on the sealing gasket 3 in the cooling zone 6, and the third connecting pipe 22 and the fourth connecting pipe 23 correspond to the positions of the two sets of isolation rings on the sealing gasket 3 in the refrigeration zone 7, under the action of the isolation rings in the cooling zone 6 and the refrigeration zone 7, the refrigerant and the cooling liquid can only enter the corresponding refrigeration zone 7 and the cooling zone 6 (that is, ensure that the refrigerant and the cooling liquid will not mix). With the continuous injection of the refrigerant and the cooling liquid, the refrigerant in the refrigeration zone 7 flows from bottom to top and is finally discharged from the second connecting pipe 21. At the same time, the cooling liquid in the cooling zone 6 flows from top to bottom and is finally discharged from the fourth connecting pipe 23. During this period, the heat of the liquids in the refrigeration zone 7 and the cooling zone 6 can be exchanged with each other through the heat conduction of the corrugated plate 10, thereby achieving the purpose of heat exchange.

[0050] Conventional heat exchangers only pass refrigerant and cooling liquid directly into the device. When the refrigerant enters the first connecting pipe 2 and enters the three groups of refrigeration zones 7 in turn, although the isolation ring on the sealing gasket 3 (the sealing gasket 3 in the cooling zone 6) can effectively isolate the cooling zone 6 to prevent the refrigerant from directly penetrating, when the refrigerant flows near the cooling zone 6, the cooling liquid will be injected into the cooling zone 6, thereby indirectly absorbing heat from the cooling liquid. At the same time, since the conventional refrigerant is liquid fluorine, and liquid fluorine will undergo a phase change (i.e., from liquid to gas) after absorbing heat, the amount of refrigerant in the cooling zone 7 that enters the refrigerant later will gradually decrease, resulting in differences in the amount of refrigerant in the three groups of refrigeration zones 7. Therefore, when the same refrigerant is injected, the difference in the amount of refrigerant will cause unevenness in the heat exchange process. Therefore, this device The following improvements have been made: a distribution pipe 25 is connected to the first connecting pipe 2, and three groups of spray valves 26 are installed at the bottom of the distribution pipe 25 through a connecting block 27 and a connecting pipe. The bottoms of the three groups of spray valves 26 are all provided with streamlined nozzles 261, and the positions of the three groups of spray valves 26 correspond to the positions of the three groups of refrigeration zones 7 respectively. When the refrigerant is passed into the first connecting pipe 2, it will first enter the distribution pipe 25 connected to the first connecting pipe 2, and under the action of the three groups of spray valves 26 at the bottom of the distribution pipe 25, it will be sprayed into the three groups of refrigeration zones 7 through the streamlined nozzles 261. Since the spray valve 26 can adjust the flow rate of the liquid, it can ensure that the pressure and flow rate of the refrigerant sprayed from each place are the same, thereby effectively ensuring that the flow rate of the refrigerant entering the three groups of refrigeration zones 7 is the same, thereby ensuring that the heat exchange conditions in each area are relatively consistent, and effectively improving the heat exchange effect.

[0051] Subsequently, the refrigerant liquid sprayed into the refrigeration zone 7 will impact the inner bottom wall of the lower guide frame 4, and under the continuous spraying of the refrigerant liquid and the shape of the lower guide frame 4, it will be sprayed on the multiple groups of first blades 43, thereby driving the multiple groups of first blades 43 located on both sides of the diverter groove 41 to rotate counterclockwise (the rotation direction is Figure 6 As shown in the figure, since the multiple groups of first blades 43 are all arranged at an angle, when the refrigerant drives them to rotate, the refrigerant itself will also be subjected to the reaction force from the first blades 43. This reaction force helps to reduce the speed at which the refrigerant is sprayed out from the liquid outlet 411 of the lower guide frame 4. At the same time, the refrigerant will collide with each other under the guidance of the multiple groups of first blades 43. This collision can prompt the refrigerant to be sprayed out from the diverter groove 41 in a more dispersed manner. The deceleration can extend the residence time of the refrigerant in the refrigeration zone 7, which means that the refrigerant has more opportunities to exchange heat with the coolant in the coolant zone 6, thereby effectively improving the heat exchange efficiency. At the same time, the mutual collision and subsequent spraying of the refrigerant at the diverter groove 41 can cause certain interference to its overall flow, thereby enhancing its turbulence intensity. Since the turbulent flow of the refrigerant has higher heat transfer efficiency and better heat absorption effect than laminar flow, the heat exchange efficiency can be further improved.

[0052] The rotation of the plurality of first blades 43 can drive the connecting shaft 421 and the first rotating shaft 42 to rotate, thereby driving the plurality of fourth blades 52 in the cooling zone 6 to rotate counterclockwise (the rotation direction is Fig.14 As shown in the figure, since the refrigerant liquid enters the second pipe 21 from the first pipe 2 and exits (i.e. from bottom to top), and the cooling liquid enters the fourth pipe 23 from the third pipe 22 and exits (i.e. from top to bottom), the plurality of fourth blades 52 are located close to the cooling liquid outflow position (i.e. the through groove corresponding to the position of the fourth pipe 23). When the cooling liquid passes into the cooling zone 6 through the third pipe 22, it will flow to the fourth blade 52 under the continuous introduction of the cooling liquid and the sequential guidance of the upper guide plate 31, the middle guide plate 32 and the lower guide plate 33 (the middle guide plate 32 can increase the residence time of the cooling liquid in the cooling zone 6 while guiding the cooling liquid so as to better exchange heat), and when the cooling liquid flows to the fourth blade 52, its flow rate It will gradually slow down due to the consumption of kinetic energy, and the turbulence intensity will be weakened. The rotation of the fourth fan blade 52 can give the coolant a kinetic energy, which is helpful to improve and maintain the turbulent state of the coolant in the coolant zone 6, thereby effectively improving the heat exchange efficiency. In addition, since the multiple groups of fourth fan blades 52 are all V-shaped structures, and the tips of the multiple groups of fourth fan blades 52 are facing the lower guide plate 33, the multiple groups of fourth fan blades 52 will rotate to push the coolant fluid guided by the lower guide plate 33 to the two groups of plate bodies constituting the coolant zone 6 (the two groups of plate bodies constituting the two outermost groups of coolant zones 6 are the side plate 1 and the corrugated plate 10, and the two groups of plate bodies constituting the two groups of coolant zones 6 in the middle are two groups of corrugated plates 10), thereby effectively improving the heat exchange efficiency and heat exchange effect.

[0053] After the refrigerant in the refrigeration zone 7 is sprayed out through the diverter groove 41 and the liquid outlet 411, it will move upward and pass through the gap between the two sets of fixed sleeves 44 and the two sets of movable blocks 441 (such as Figure 8 As shown in the figure, when the refrigerant passes through the gap between the two groups of fixed sleeves 44 and the two groups of movable blocks 441, the refrigerant will apply a pressure to the two groups of movable blocks 441 when the movable blocks 441 are set at an angle toward the fixed sleeve 44, so that the two groups of movable blocks 441 move away from each other until the two groups of movable blocks 441 contact the two groups of corrugated plates 10 in the refrigeration zone 7. At this time, the spring 443 is compressed, and its elastic force generates a pulling force on the two groups of fixed sleeves 44, thereby indirectly applying a force in the opposite direction to the corrugated plates 10, thereby ensuring that the two groups of corrugated plates 10 in the refrigeration zone 7 can effectively prevent the leakage of the refrigerant even if they face a large internal impact (i.e., the impact of the refrigerant), thereby effectively ensuring the smooth progress of the heat exchange process.

[0054] After passing through the gap between the diverter groove 41 and the movable block 441, the refrigerant will come to the liquid inlet 452. At this time, its flow rate will gradually slow down due to the consumption of kinetic energy, and the turbulence will weaken. Therefore, its flow rate is not as good as that of the coolant at the same height. Therefore, it is necessary to convert part of the kinetic energy of the coolant to the refrigerant to improve the turbulence effect of the refrigerant at this location. Since the six groups of corrugated plates 10 are all installed with an adapter box 13, and the adapter box 13 is provided with a small gear 131 and a large gear 132 and meshes with each other, and the second rotating shaft 46 is fixedly connected to the small gear 131, and the third rotating shaft 5 is fixedly connected to the large gear 132, therefore, when the coolant in the cooling zone 6 flows to the multiple groups of third blades 51 under the guidance of the upper guide plate 31, it will push the multiple groups of third blades 51 and make the multiple groups of third blades 51 and the third rotating shaft 5 start to rotate clockwise (the direction of rotation is Fig.13 As shown in the figure, the large gear 132, the small gear 131, the second rotating shaft 46 and the plurality of second blades 461 on the second rotating shaft 46 can be driven to rotate in sequence. Since the large gear 132 and the small gear 131 are meshed with each other, the plurality of second blades 461 in the refrigeration zone 7 rotate counterclockwise (the rotation direction is Fig.10 As shown in the figure, the rotation of the plurality of second blades 461 can draw the refrigerant into the upper guide frame 45, and move it upward to the inner top wall of the upper guide frame 45 through the baffle plate 451, and finally be discharged through the through groove on the corrugated plate 10 and the second connecting pipe 21.

[0055] Since the multiple sets of third fans are all arranged in a straight manner, they can better absorb the kinetic energy of the cooling liquid to increase its rotation speed, that is, effectively increase the rotation speed of the second fan blade 461, and since the diameter of the small gear 131 is smaller than that of the large gear 132, the angular velocity of the small gear 131 will be faster when the linear velocity is the same through meshing (that is, the rotation speed of the third fan blade 51 is smaller than that of the second fan blade 461), thereby further increasing the rotation speed of the second fan blade 461, and then effectively improving the turbulent effect of the refrigerant at the second fan blade 461 in the refrigeration zone 7, that is, effectively improving the heat exchange efficiency. Since liquid fluorine (refrigerant) will change from liquid to gas after absorbing heat, and the heat absorption capacity of gaseous fluorine is weaker than that of liquid fluorine, it is necessary to discharge the gaseous fluorine from the refrigeration zone 7 as soon as possible to avoid reducing the heat exchange efficiency. When the gas-liquid mixture of fluorine (that is, the mixture of liquid fluorine and gaseous fluorine) passes through the second fan blade 461, due to the multiple sets of second fan blades 46 1 rotates, the gas-liquid mixture is accelerated and moves along the rotation direction of the second rotating shaft 46. At this time, since the density of the liquid is greater than that of the gas, and the second fan blade 461 adopts a V-shaped structure and is arranged in a curved shape, the liquid fluorine will be mostly concentrated in the depression on the second fan blade 461 under the action of its own density and inertia, while the gaseous fluorine is squeezed to the two sides of the second fan blade 461 and moves upward due to its smaller density. Due to the existence of the baffle plate 451, the gaseous fluorine is diverted when flowing through the baffle plate 451, and moves upward from the two sides of the baffle plate 451, and is finally discharged through the through groove and the second connecting pipe 21, while the liquid fluorine is more retained near the second fan blade 461, and only a small part moves upward with the gaseous fluorine and is discharged through the through groove and the second connecting pipe 21. This design not only improves the heat exchange time between the liquid fluorine (refrigerating liquid) and the cooling liquid in the cooling zone 6, but also accelerates the discharge of the gaseous fluorine, thereby further improving the heat exchange efficiency.

[0056] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims

1. A plate heat exchanger with plug-in type forced flow optimization distribution, comprising two groups of side plates (1) and six groups of corrugated plates (10), wherein the two groups of side plates (1) and the six groups of corrugated plates (10) are all provided with four groups of through grooves, wherein the four groups of through grooves on one group of the side plates (1) are respectively detachably mounted with a first pipe (2), a second pipe (21), a third pipe (22) and a fourth pipe (23) on the outward side, wherein the second pipe (21) is located directly above the first pipe (2), and the third pipe (22) is located directly above the fourth pipe (23), and the four groups of through grooves on the other group of the side plates (1) are detachably mounted with sealing plugs (24) on the outward side, characterized in that: Also includes: A fixing mechanism, the fixing mechanism being arranged on the two groups of side plates (1) and the six groups of corrugated plates (10) and being used for pressing and fixing the two groups of side plates (1) and the six groups of corrugated plates (10); Seven groups of sealing gaskets (3), wherein five groups of the sealing gaskets (3) are respectively inserted between two adjacent groups of corrugated plates (10) among the six groups of corrugated plates (10), and the other two groups of the sealing gaskets (3) are respectively inserted between two groups of side plates (1) and two adjacent groups of corrugated plates (10), and two adjacent groups of sealing gaskets (3) among the seven groups of sealing gaskets (3) are arranged in opposite directions to each other, and the areas where the two adjacent groups of sealing gaskets (3) are located are the cooling zone (6) and the refrigeration zone (7), respectively. The sealing gaskets (3) are arranged in a trapezoidal shape inclined at 90 degrees, and isolation rings are installed on the edges of the top and bottom ends of the sealing gaskets (3) that are inclined downward, the first connecting pipe (2) and the second connecting pipe (21) correspond to the positions of the two groups of isolation rings on the sealing gasket (3) in the cooling zone (6), and the third connecting pipe (22) and the fourth connecting pipe (23) correspond to the positions of the two groups of isolation rings on the sealing gasket (3) in the refrigeration zone (7); a liquid separation mechanism, the liquid separation mechanism being arranged on the first connecting pipe (2) and a set of sealing plugs (24) corresponding thereto, and being used to make the flow rate of the refrigerant liquid entering the refrigeration zone (7) uniform; A first auxiliary mechanism and a second auxiliary mechanism, wherein the first auxiliary mechanism and the second auxiliary mechanism are both arranged in the seven groups of sealing gaskets (3), the cooling zone (6) and the refrigeration zone (7) are both provided with fan blades, and the fan blades located in the cooling zone (6) and the refrigeration zone (7) are respectively arranged on the first auxiliary mechanism and the second auxiliary mechanism, and the fan blades located in the refrigeration zone (7) of the first auxiliary mechanism rotate under the impact of the refrigerant entering the refrigeration zone (7) and reduce the flow rate of the refrigerant initially entering the refrigeration zone (7), and at the same time, through the transmission effect, the fan blades located in the cooling zone (6) of the first auxiliary mechanism rotate and give kinetic energy to the cooling liquid that is about to flow out of the cooling zone (6); The fan blades located in the cooling zone (6) of the second auxiliary mechanism rotate under the impact of the cooling liquid entering the cooling zone (6) and reduce the flow rate of the cooling liquid initially entering the cooling zone (6). At the same time, through the transmission effect, the fan blades located in the refrigeration zone (7) of the second auxiliary mechanism rotate and give kinetic energy to the refrigeration liquid that is about to flow out of the refrigeration zone (7).

2. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 1, characterized in that: The area where the sealing gasket (3) is located near the side plate (1) is a cooling zone (6). There are seven groups of cooling zones (6) and refrigeration zones (7), four groups of cooling zones (6) and three groups of refrigeration zones (7). A group of sealing sheets (14) is detachably installed at the installation position of the first connecting pipe (2) and the side plate (1), and another group of sealing sheets (14) is detachably installed at the installation position of the sealing plug (24) opposite to the first connecting pipe (2) and the side plate (1).

3. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 2, characterized in that: The fixing mechanism comprises four groups of fixing columns (11), the four groups of fixing columns (11) respectively penetrate and are inserted into four groups of corners on the two groups of side plates (1) and the six groups of corrugated plates (10), and fixing nuts (12) are detachably mounted on both ends of the four groups of fixing columns (11). The liquid dispensing mechanism comprises a distribution pipe (25), the end of the first connecting pipe (2) facing the side plate (1) is closed, one end of the distribution pipe (25) penetrates and is inserted into the end of the first connecting pipe (2) facing the side plate (1), and the other end of the distribution pipe (25) passes through the two groups of side plates (1) and the six groups of corrugated plates (10) and is connected to the first connecting pipe (25). 2) and is detachably mounted on the inward end of a sealing plug (24) corresponding to the first connecting pipe (2); the bottom end of the distribution pipe (25) is fixedly connected to a connecting block (27); three groups of liquid spray valves (26) are fixedly mounted on the connecting block (27); the top ends of the three groups of liquid spray valves (26) are all equipped with connecting pipes, and the three groups of liquid spray valves (26) are all connected to the inside of the distribution pipe (25) through the connecting pipes; the bottom ends of the three groups of liquid spray valves (26) are all provided with streamlined nozzles (261), and the positions of the three groups of liquid spray valves (26) correspond to the positions of the three groups of refrigeration zones (7), respectively.

4. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 3, characterized in that: The first auxiliary mechanism comprises a flow reduction component and three groups of lower flow guide frames (4). The three groups of lower flow guide frames (4) are respectively inserted between two groups of corrugated plates (10) of the three groups of refrigeration zones (7). The positions of the three groups of lower flow guide frames (4) correspond to the positions of the first connecting pipes (2). The inner side walls of the three groups of lower flow guide frames (4) facing the isolation ring are penetrated by a liquid outlet (411). The position of the liquid outlet (411) is close to the top of the lower flow guide frame (4). The flow reduction component is arranged in the three groups of refrigeration zones (7) for interfering with the refrigerant initially entering the refrigeration zones (7). The energy enhancement component is arranged in the four groups of cold-carrying zones (6) for giving kinetic energy to the cold-carrying liquid that is about to flow out of the cold-carrying zones (6).

5. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 4, characterized in that: The flow reduction assembly comprises two groups of first rotating shafts (42) and two groups of connecting side shafts (421), wherein the two groups of first rotating shafts (42) are located between the two groups of connecting side shafts (421), and the outward ends of the two groups of connecting side shafts (421) are respectively rotatably connected to the inner side walls of the two groups of side plates (1), and the inward ends of the two groups of connecting side shafts (421) penetrate a group of corrugated plates (10) and extend respectively into a group of refrigeration zones (7), wherein one group of the first rotating shafts (42) penetrates and is rotatably connected to the inner side walls of the two groups of side plates (1). On two of the four groups of corrugated plates (10) located in the middle, another group of the first rotating shafts (42) penetrates and is rotatably connected to the other two groups of corrugated plates (10) located in the middle, the two groups of the first rotating shafts (42) are symmetrical to each other, and the opposite ends of the two groups of the first rotating shafts (42) are located in one refrigeration zone (7), and the non-opposite ends of the two groups of the first rotating shafts (42) are respectively connected to the two groups of connecting side shafts (421 ) are located in the same group of refrigeration zones (7) at one end facing inwards of the two groups of connecting shafts (421) located in the refrigeration zones (7), and multiple groups of first fan blades (43) are fixedly connected to the outer walls of the two ends of the two groups of first rotating shafts (42) located in the refrigeration zones (7), and the multiple groups of first fan blades (43) in the three groups of refrigeration zones (7) are respectively located in the three groups of lower guide frames (4), and the positions of the multiple groups of first fan blades (43) in the three groups of refrigeration zones (7) are aligned with the positions of the multiple groups of first fan blades (43) in the three groups of lower guide frames (4). The positions of the liquid ports (411) correspond to each other, the plurality of groups of the first blades (43) are all arranged in an inclined manner, the side walls of the three groups of the lower guide frames (4) are provided with flow diversion grooves (41) near the positions of the plurality of first blades (43), the opposite ends of the two groups of the first rotating shafts (42) are respectively located on both sides of one group of flow diversion grooves (41), and the non-opposite ends of the two groups of the first rotating shafts (42) and the inward ends of the two groups of the connecting side shafts (421) are respectively located on both sides of the other two groups of flow diversion grooves (41).

6. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 5, characterized in that: The energy boosting assembly comprises four groups of lower guide plates (33), wherein two groups of the lower guide plates (33) are respectively inserted between two groups of corrugated plates (10) of two groups of refrigeration zones (7), and the other two groups of the lower guide plates (33) are respectively inserted between a group of side plates (1) and a group of corrugated plates (10) of the other two groups of refrigeration zones (7). The heights of the four groups of lower guide plates (33) are all between the third connecting pipe (22) and the fourth connecting pipe (23). A plurality of groups of fourth blades (52) are installed at the middle positions of the outer walls of the two groups of the first rotating shafts (42) and the two groups of connecting side shafts (421). The plurality of fourth blades (52) on the outer walls of the first rotating shaft (42) and the two sets of connecting shafts (421) are respectively located in the four sets of cooling zones (6); the plurality of fourth blades (52) are all V-shaped structures; the plurality of fourth blades (52) located in the cooling zone (6) are located close to the isolation ring position on the sealing gasket (3) in the cooling zone (6); and the tips of the plurality of fourth blades (52) are oriented toward the lower guide plate (33); one end of the lower guide plate (33) is in contact with the inner wall of one side of the sealing gasket (3); and the other end of the lower guide plate (33) is close to the plurality of fourth blades (52).

7. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 6, characterized in that: The second auxiliary mechanism comprises three groups of upper flow guide frames (45), the three groups of upper flow guide frames (45) are respectively inserted between two groups of corrugated plates (10) of the three groups of refrigeration zones (7), and the three groups of upper flow guide frames (45) are respectively located directly above the three groups of lower flow guide frames (4), the positions of the three groups of upper flow guide frames (45) all correspond to the positions of the second connecting pipes (21), and the inner side walls of the three groups of upper flow guide frames (45) facing the isolation ring are penetrated by liquid inlets (452), the The liquid inlet (452) is located near the bottom end of the upper guide frame (45), and a baffle (451) is fixedly installed at the middle position of the inner wall of the three groups of upper guide frames (45), and the width of the baffle (451) is smaller than the width of the upper guide frame (45). The three groups of refrigeration zones (7) and the four groups of cooling zones (6) are commonly provided with a deceleration and energy-increasing component for giving kinetic energy to the cooling liquid that is about to flow out of the refrigeration zone (7) and interfering with the cooling liquid that has just entered the cooling zone (6).

8. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 7, characterized in that: The deceleration and energy boosting assembly comprises six groups of adapter boxes (13), two groups of edge shells (130), three groups of second rotating shafts (46) and four groups of third rotating shafts (5); the two groups of edge shells (130) penetrate through and are detachably mounted on the two groups of side plates (1), and the two groups of edge shells (130) correspond to the positions of the six groups of adapter boxes (13); the six groups of adapter boxes (13) penetrate through and are detachably mounted on the six groups of corrugated plates (10), respectively; the three groups of second rotating shafts (46) are respectively located in the three groups of refrigeration zones (7), and the two ends of the three groups of second rotating shafts (46) respectively penetrate through the outer side walls of two adjacent groups of adapter boxes (13) among the six groups of adapter boxes (13); The second rotating shaft (46) of each group is respectively located between each two groups of the third rotating shaft (5), and the four groups of the third rotating shaft (5) are located in the four groups of cooling zones (6). The two ends of the two groups of the third rotating shaft (5) respectively penetrate the outer side walls of two adjacent groups of the four groups of the switching boxes (13) located in the middle, and are rotatably connected to the corresponding switching boxes (13). The outward ends of the other two groups of the third rotating shaft (5) are respectively rotatably connected to the two groups of edge shells (130), and the inward ends of the two groups of the third rotating shaft (5) respectively penetrate the outer side walls of the two outermost groups of the switching boxes (13), and are rotatably connected to the corresponding switching boxes (13). The three groups of second rotating shafts (46) are rotatably connected to the corresponding adapter boxes (13), the three groups of second rotating shafts (46) are all located above the four groups of third rotating shafts (5), and multiple groups of second fan blades (461) are fixedly connected to the outer walls of the three groups of second rotating shafts (46), the multiple groups of second fan blades (461) are all V-shaped structures, and the multiple groups of second fan blades (461) are all arranged in a curved shape, the multiple groups of second fan blades (461) on the three groups of second rotating shafts (46) are respectively located in the three groups of upper guide frames (45), and the positions of the multiple groups of second fan blades (461) on the three groups of second rotating shafts (46) correspond to the positions of the liquid inlets (452) in the three groups of upper guide frames (45), and the multiple groups of second fan blades (461) on the three groups of second rotating shafts (46) correspond to the positions of the liquid inlets (452) in the three groups of upper guide frames (45). The second fan blade (461) is located below the spoiler (451) on the upper guide frame (45); multiple groups of third fan blades (51) are fixedly connected to the outer walls of the four groups of third rotating shafts (5); the multiple groups of third fan blades (51) are arranged in a straight manner; the multiple groups of third fan blades (51) in each group of the cooling zone (6) are located directly above the multiple groups of fourth fan blades (52) in each group of the cooling zone (6); and large gears (132) and small gears (131) are respectively installed on the outer walls of the third rotating shafts (5) and the second rotating shafts (46) located in the six groups of the adapter boxes (13); the large gears (132) and small gears (131) are meshed with each other.

9. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 8, characterized in that: Each of the four groups of cooling zones (6) is provided with a group of upper guide plates (31) and a group of middle guide plates (32); two groups of upper guide plates (31) among the four groups of upper guide plates (31) and two groups of middle guide plates (32) among the four groups of middle guide plates (32) are respectively inserted between two groups of corrugated plates (10) of the two groups of cooling zones (7); and the other two groups of upper guide plates (31) and the other two groups of middle guide plates (32) are respectively inserted between a group of side plates (1) and a group of corrugated plates (10) of the other two groups of cooling zones (7). The upper guide plate (31) is located above the lower guide plate (33), the middle guide plate (32) is located between the upper guide plate (31) and the lower guide plate (33), one end of the upper guide plate (31) is in contact with the inner wall of one side of the sealing gasket (3), and the other end of the upper guide plate (31) is close to the plurality of groups of third blades (51), one end of the middle guide plate (32) is in contact with the inner wall of the other side of the sealing gasket (3), and the middle guide plate (32) is located between the plurality of groups of third blades (51) and the plurality of groups of fourth blades (52).

10. The plate heat exchanger with plug-in type forced flow optimization distribution according to claim 2, characterized in that: The invention also comprises three groups of stabilizing mechanisms, which are respectively arranged in the three groups of refrigeration zones (7). The stabilizing mechanisms comprise two groups of fixing sleeves (44), which are respectively fixedly installed at the middle positions of the two opposite sides of the two groups of corrugated plates (10) in the refrigeration zone (7), and both ends of the two groups of fixing sleeves (44) are in contact with the inner side wall of the sealing gasket (3) in the refrigeration zone (7). One group of the fixing sleeves (44) is located above the other group of the fixing sleeves (44), and two groups of sliding grooves are respectively opened in the fixing sleeves (44) near the edges of the two ends. The two groups of sliding grooves are sealed and slidably connected with sliders. The two groups of sliding grooves are sealed and slidably connected with the sliders. The blocks are both provided with movable rods (442), the ends of the two sets of movable rods (442) away from the slider penetrate the inner wall of the slide groove and are fixedly connected with the movable block (441) together, the part of the movable rod (442) located in the slide groove is sleeved with a spring (443), one end of the spring (443) is fixedly connected to the slider, and the other end of the spring (443) is fixedly connected to the inner wall of the slide groove, the two sets of movable blocks (441) are both arranged in an oblique angle toward the two sets of fixed sleeves (44), and there are gaps between the two sets of corrugated plates (10) and the two sets of fixed sleeves (44) on the sides of the two sets of movable blocks (441) away from the two sets of fixed sleeves (44).

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