TW202043693A - Inlet distributor for plate heat exchanger to achieve the objective of uniform distribution of liquid and vapor mixed at medium and low flow rates and the effect of indeed effectively enhancing the overall heat transfer performance - Google Patents

Abstract

This invention provides an inlet distributor for a plate heat exchanger. The plate heat exchanger comprises a plate set, fluid channels formed between the plates, and a plurality of first fluid openings and second fluid openings provided on the plates to form multiple inlet pipes and outlet pipes for the fluid to alternately enter and discharged from the fluid channels. The inlet distributor comprises a header pipe and at least one horizontal baffle disposed on the pipe wall of the header pipe. The header pipe can be installed at the inlet end of the inlet pipe. The horizontal baffle can be extended coaxially into the inlet pipe. When the fluid flows into the header pipe, the two-phase liquid and vapor of the passing fluid can be separated by the horizontal baffle first, making the vapor guided along the horizontal baffle to the fluid channel at different positions away from the inlet end, so as to achieve the objective of uniform distribution of liquid and vapor mixed at medium and low flow rates, and the effect of indeed effectively enhancing the overall heat transfer performance due to the small pressure drop increase of the fluid caused by the horizontal baffle.

Description

Inlet distributor for plate heat exchanger

The present invention provides an inlet distributor for a plate heat exchanger, in particular, the horizontal baffle of the distributor can be used to first separate the two-phase liquid and vapor of the fluid passing through the header, and then guide the vapor to the plate The heat exchanger is far away from the fluid channel at different positions at the inlet end to achieve the effect of uniform distribution of liquid and vapor mixing at medium and low flow rates and increased heat transfer performance.

According to, in recent years, plate heat exchangers have been widely used in refrigeration, refrigeration and air conditioning, heat pump systems, heat treatment, petrochemicals, energy, waste heat recovery and other industries. Its structure and working principle are stacked with metal sheets with certain corrugated shapes. With the formation of fluid channels between the plates, the heat transfer properties of the plates can be used to exchange heat between two fluids (such as liquid to liquid or liquid to vapor) to achieve the purpose of heating or cooling. It has the advantages of compact structure, high heat transfer efficiency, small size and easy maintenance and inspection.

As shown in Figure 10, the plate heat exchanger A includes a plate group A1, and a fluid channel A10 is formed between each two adjacent plates of the plate group A1, and each plate is at four corners. The corresponding opening on the upper part is formed with a plurality of inlet pipes A2 and outlet pipes A3 for the fluid B to enter and discharge the fluid passage A10 for heat exchange. In practical applications, the fluid B of the plate heat exchanger A is usually two-phase (liquid and Vapour) mixed instead of single-phase fluid. When two-phase fluid (such as refrigerant) flows in through the inlet header of plate heat exchanger A, due to the liquid (such as liquid The inertial force and gravity of the refrigerant) are greater than that of steam (such as vapor refrigerant), and the momentum of the liquid is much greater than that of the steam, causing most of the liquid to flow forward to the back end of the plate heat exchanger A away from the inlet header. In the inlet pipe A2, most of the steam flows upward in the inlet pipe A2 near the front-end inlet header of the plate heat exchanger A, causing uneven flow distribution of liquid and steam into each fluid channel A10 and affecting the whole The heat transfer performance, thereby reducing the heat exchange efficiency of the plate heat exchanger A.

Therefore, in order to solve the problem of uneven fluid distribution at the inlet of the flow channel of the plate heat exchanger, currently most of them are provided with a distributor at the inlet of the flow channel, and the existing distributor is used to reduce the area of the fluid inlet, thereby limiting The flow rate into the flow channel, or to increase the flow rate of the fluid in the flow channel, is expected to achieve the goal of uniform fluid distribution in the flow channel, but the design of the inlet distributor will not only affect the flow of fluid into the plate heat exchanger The pressure drop generated at the time will have an absolute impact on the uniformity of the fluid distribution between the various flow channels. When the number of plates in the plate heat exchanger is large, the pressure drop will be concentrated at the inlet of the flow channel, so The pressure drop at the inlet of the flow channel is also an important factor in determining whether the overall heat transfer performance of the plate heat exchanger is good. The existing distributor reduces the area design of the fluid inlet, although it can effectively increase the flow rate of the fluid in the flow channel, but the flow The pressure drop also increases relatively, but it will affect the flow and cause unnecessary pressure loss. At the same time, it will cause uneven fluid distribution, which will affect the overall heat transfer performance. It needs to be redesigned by those engaged in this industry to effectively solve it.

Therefore, in view of the above-mentioned conventional problems and deficiencies, the inventor collected relevant information through multiple evaluations and considerations, and used many years of research and development experience in this industry to design, and only this type of inlet distributor for plate heat exchangers The invention patent was born.

The main purpose of the present invention is that the plate heat exchanger is located between each two adjacent plates of the plate group to form a fluid channel, and has a plurality of first fluid openings and second fluid openings on the plates to form a fluid supply A plurality of inlet pipes and outlet pipes that alternately enter and discharge fluid channels for heat exchange, and the inlet distributor includes a header and at least one horizontal baffle arranged on the pipe wall of the header to collect The pipe and the horizontal baffle are installed at the inlet end of the inlet pipe, and the horizontal baffle extends coaxially into the inlet pipe. When the fluid flows into the header, the two-phase liquid and vapor of the passing fluid can be first passed by the horizontal baffle. After separation, the vapor is guided along the horizontal baffle to the fluid channel at different positions away from the inlet end, so that the liquid and vapor are mixed and distributed evenly at medium and low flow rates, and the horizontal baffle is made of sheet metal ( For example, thin steel sheet) causes a small increase in fluid pressure drop, which can indeed effectively improve the overall heat transfer performance.

The secondary purpose of the present invention is that the inlet distributor can be based on the characteristics that the liquid will be distributed on the pipe wall when the fluid is two-phase liquid and vapor flowing at a high speed, so that the fluid can pass through the manifold and use multiple pieces of different lengths. The baffle separates the two-phase liquid and vapor of the fluid, and then guides them to different positions in the plate heat exchanger, thereby controlling the flow of fluid into the fluid channel, and the number and length of each horizontal baffle can be adjusted. Depending on the size of the plate heat exchanger, or the size of the inlet end of the inlet pipe and the size of the opening area formed by the pipe of the header, one or more horizontal baffles are provided, or according to the plate heat exchanger or plate group The total length and the number of stacked pieces can be adjusted for adaptability.

1‧‧‧ Collector

11‧‧‧Pipe

111‧‧‧First opening

112‧‧‧Second opening

2‧‧‧Horizontal partition

3‧‧‧Plate heat exchanger

31‧‧‧Plate Group

310‧‧‧Fluid channel

311‧‧‧Plate

312‧‧‧First fluid opening

313‧‧‧Second fluid opening

32‧‧‧Inlet pipe

321‧‧‧Entrance

33‧‧‧Export pipeline

331‧‧‧Exit port

34‧‧‧Front Panel

341‧‧‧First fluid interface

342‧‧‧Second fluid interface

35‧‧‧Back Panel

4‧‧‧Fluid

A‧‧‧Plate heat exchanger

A1‧‧‧Plate Group

A10‧‧‧Fluid channel

A2‧‧‧Inlet pipe

A3‧‧‧Exit pipe

B‧‧‧Fluid

The first figure is a schematic cross-sectional view of the plate heat exchanger of the present invention with an inlet distributor installed.

The second figure is a partial enlarged view of part A of the first figure of the present invention.

The third figure is a front view of the plate heat exchanger of the present invention.

The fourth figure is a perspective view of the inlet distributor of the preferred embodiment of the present invention.

Figure 5 is a front view of the inlet distributor of the preferred embodiment of the present invention.

Figure 6 is a perspective view of the entrance distributor of another preferred embodiment of the present invention.

The seventh figure is a front view of another preferred embodiment of the inlet distributor of the present invention.

The eighth diagram is a comparison diagram of the influence of the installation of the inlet distributor on the pressure drop of the refrigerant according to the present invention.

The ninth figure is a comparison diagram of the influence of the inlet distributor of the present invention on the heat transfer coefficient of the refrigerant.

Figure 10 is a schematic cross-sectional view of a conventional plate heat exchanger.

In order to achieve the above-mentioned purpose and effect, the technical means and structure adopted by the present invention are illustrated in detail below to explain the structure and function of the preferred embodiment of the present invention in order to fully understand.

Please refer to the first, second, third, fourth, and fifth drawings, which are respectively a cross-sectional schematic diagram of the plate heat exchanger of the present invention with an inlet distributor installed, a partial enlarged view of part A of the first figure, and a front view of the plate heat exchanger Figure. The perspective view of the inlet distributor of the preferred embodiment and the front view of the inlet distributor. It can be clearly seen from the figure that the inlet distributor for the plate heat exchanger of the present invention includes: a header 1, A pipe 11 is formed inside the header 1, and a first opening 111 and a second opening 112 are respectively formed at the two ends of the pipe 11; and at least one horizontal partition plate 2 is in the shape of a long rectangular sheet and is made of stainless steel, It is made of iron, iron-palladium, nickel or nickel-based alloys (such as nickel, molybdenum, chromium alloys), and the horizontal partition 2 can be welded, riveted, or riveted at the short side at one end or the two long sides at the opposite end. Mosaic card Or other combined methods are arranged on the inner wall surface of the pipe 11 or the second opening 112, and the other end of each horizontal partition plate 2 extends out of the pipe 11 to form a suspended state.

The above-mentioned inlet distributor of the present invention can be applied to refrigeration (used as a condenser and evaporator), HVAC (such as an intermediate heat exchanger used with boilers or high-rise buildings), industry (such as machinery, metallurgy, gas turbines) , Electric power, etc.) use cooling and heating equipment or other occasions where the plate heat exchanger 3 is required for heating or cooling, wherein the plate heat exchanger 3 includes a plate group 31 arranged face to face at intervals, and the plate group 31 A fluid channel 310 separated from each other is formed between each two adjacent plates 311, and each plate 311 has a corresponding plurality of first fluid openings 312 and second fluid openings 313 at four corners, and each two The adjacent plates 311 can also be further provided with gaskets for sealing, or can be integrated by direct plate-to-plate welding, so that multiple first fluid openings 312 and second fluid openings 313 can be formed for more than one type Fluid 4 (such as water, refrigerant, water-to-refrigerant or other working fluids with a two-phase mixture of liquid and vapor, etc.) alternately enters and discharges the multiple inlet pipes 32 and outlet pipes 33 of the fluid channel 310 for heat exchange, while ensuring that each The closeness between the plates 311 does not cause side leakage or lack of communication, and the plate group 31 can also be fixed on the front end plate 34 and the rear end plate 35 through a frame (such as upper and lower support frames) and bolts. The front end plate 34 has a plurality of first fluid ports 341 and second fluid ports 342 corresponding to the inlet pipe 32 and the outlet pipe 33 respectively.

When the fluid 4 flows into the inlet end 321 of the inlet pipe 32 through the first fluid interface 341 under the front end plate 34, and alternately flows through the first fluid openings 312 of the plate group 31 under each plate 311 into the fluid channel 310 After inside, it can be discharged from the first fluid opening 312 above the plate 311 into the outlet pipe 33, and then through the outlet end 33 1 and the first fluid port 341 above the front end plate 34 to form a first flow path for the fluid 4 to enter and exit the plate heat exchanger 3; similarly, when another fluid 4 passes through the second fluid port above the front end plate 34 342 flows into the inlet end 321 of the other inlet pipe 32, and alternately flows through the second fluid openings 313 of the plate group 31 above each plate 311 and flows into the fluid channel 310, and then flows from the second fluid under the plate 311 The fluid opening 313 is discharged into the other outlet pipe 33, and then discharged through the outlet end 331 and the second fluid interface 342 under the front end plate 34 to form a second flow channel for the entry and discharge of another fluid 4, and the first flow The channel and the second flow channel are not connected to each other.

In this embodiment, the plate type heat exchanger 3 adopts the type of plate 311 that can be mountain-shaped, Z-shaped, or protruding and recessed, and is not limited to this, and the plate heat exchanger 3 may be designed according to different designs. Different types (such as plate heat exchangers with sealing gaskets, welded plate heat exchangers, spiral plate heat exchangers or plate coil heat exchangers, etc.) and the number of plates 311 can be provided, and the detailed structure is not the case The key point of the appeal is that it only needs to provide the plate heat exchanger 3 that can utilize the heat transfer properties of multiple metal plates 311 to quickly heat or cool the fluid 4 through at least two unconnected flow channels for heat exchange. Therefore, The contents of the following instructions in this case are all explained together, and they are submitted to Chen Ming.

When the present invention is assembled, the header 1 of the inlet distributor is first installed on the inlet end 321 of one of the inlet pipes 32 at the bottom of the plate heat exchanger 3 by welding, screw locking or other methods, or The front end plate 34 is connected to the inlet end 321 in the first fluid interface 341, and the other end of the horizontal partition plate 2 extending from the second opening 112 is coaxially penetrated into the inlet pipe 32, and the plate of the horizontal partition plate 2 The surface corresponds to the plurality of fluid channels 310 of the plate group 31, and the whole assembly of the present invention is completed.

In this embodiment, when the fluid 4 flows into the plate heat exchanger 3 through the first fluid interface 341 of the front plate 34, an inlet distributor can be used to install at the inlet end 321 of the inlet pipe 32, according to the fluid 4 The characteristics of two-phase liquid and vapor (such as steam) that the liquid will be distributed on the pipe wall when flowing at high speed. After the fluid 4 passes through the pipe 11 of the header 1 at the inlet end 321, at least one horizontal partition can be used 2 First, separate the two-phase liquid and vapor of the fluid 4 so that more vapor flows into the upper and lower sides of each horizontal partition 2 (as shown in the second figure), and the vapor flows along the horizontal partition. The plate 2 is guided to the fluid channels 310 at different positions of the inlet pipe 32 away from the inlet end 321, so as to control the flow rate of the liquid and vapor into each fluid channel 310 after mixing, so that the fluid 4 is evenly distributed in each fluid channel 310 The purpose is to significantly increase the overall heat transfer performance, and because the horizontal partition 2 is made of a thin stainless steel material, the pressure drop caused by the fluid 4 under high flow or viscous conditions can be reduced to be effective Improve the heat exchange efficiency of the plate heat exchanger.

Furthermore, the number of plates 311 of the plate group 31 of the plate heat exchanger 3 can preferably be 20 to 70, but in practical applications, different numbers of plates can be provided according to the different designs of the plate heat exchanger 3. And 60 fluid channels 310 are formed between the plate group 31, the front end plate 34 and the rear end plate 35, and an inlet distributor is installed at the inlet end 321 of the inlet pipe 32, and the header 1 of the inlet distributor In the vertical direction, the inner wall can be provided with two non-equidistantly distributed horizontal partitions 2, and the two horizontal partitions 2 separate the pipes 11 to form three openings of different areas for the passage of fluid 4, so that fluid 4 can pass through. Three flow streams are generated when passing through, and the area size relationship of each opening can also be adjusted appropriately with the number of horizontal partitions 2, so as to restrict the fluid 4 from being guided to the inlet pipe 32 along the multiple horizontal partitions 2 Flow, or increase the flow rate, so that the fluid 4 can be more evenly distributed.

In addition, the upper and lower horizontal baffles 2 of the above-mentioned inlet distributor in the header 1 respectively extend from the inlet end 321 of the plate heat exchanger 3 to the positions of the 20th and 40th fluid channels 310, and make The length L1 of the upper horizontal partition 2 is shorter than the length L2 of the lower horizontal partition 2. However, in practical applications, multiple horizontal partitions 2 can also be arranged in the header 1, and the horizontal partition 2 The length increases sequentially from top to bottom, and the length of the horizontal partition 2 is proportional to the number of plates 311 of the plate group 31; also, in this embodiment, between the upper and lower horizontal partitions 2 To be separated by a distance D1, and to make the two horizontal partitions 2 and the wall of the pipe 11 have the maximum distance D2 and D3 in the vertical direction, and the distance D1 between the two horizontal partitions 2 is greater than the upper horizontal partition 2 and the pipe The maximum distance D2 formed by the wall 11 in the vertical direction, but the distance D1 is smaller than the maximum distance D3 formed by the horizontal partition 2 and the wall of the pipe 11 in the vertical direction, which can be distributed non-equidly in the header 1 The two horizontal partitions 2 are used to restrict the flow rate of the fluid 4 or increase its flow rate.

Please also refer to Figures 6 and 7 respectively, which are respectively the three-dimensional appearance and front views of the inlet distributor of another preferred embodiment of the present invention. It can be clearly seen from the figures that the inlet distributor of the present invention is similar to the above The structure of the inlet distributor in the fourth and fifth figures is roughly the same, wherein the inner wall of the header 1 is provided with two equally spaced horizontal partitions 2 in the vertical direction, and is formed by the two horizontal partitions 2 separating the pipe 11 There are three openings of the same area for the passage of fluid 4, so the two structures are mainly only different in the size of the opening area formed by the header 1 separated by the horizontal partition 2, that is, the distance D1 between the upper and lower horizontal partitions 2 is equal to the above The distance D2 between the horizontal partition 2 and the wall of the pipe 11 is equal to the distance D3 between the lower horizontal partition 2 and the wall of the pipe 11, so that the fluid 4 forms a stable layer when flowing through the horizontal partition 2 in the inlet pipe 32 Flow state, and the pressure drop increase is small.

In addition, the above-mentioned inlet distributor is provided with at least one horizontal partition plate 2 on the wall surface of the pipe 32 of the header 1, and the header 1 is installed on the plate heat exchanger 3 at the inlet end of the inlet pipe 32 for the fluid 4 to flow in. 321, and each horizontal partition 2 extends coaxially into the inlet pipe 32 by extending the pipe 32, and the number of horizontal partitions 2 can be provided with one or more horizontal partitions 2 according to the size of the inlet end 321 of the inlet pipe 32 , And the length of each horizontal partition plate 2 can be adjusted in proportion to the number of plates 311 of the plate group 31, and the length of the horizontal partition plate 2 can also be a plate heat exchanger 3 or 1/3 to 2/3 of the total length of the plate group 31. For example, the length of the two horizontal partitions 2 provided in the header 1 can be preferably 1/3 and 2/ of the total length of the plate group 31. 3. In this embodiment, the horizontal partition 2 is a thin steel sheet, but in actual application, it is not limited to this. For example, simple modifications and equivalent structural changes made by using the specification and drawings of the present invention , Should be included in the scope of the patent of the present invention for the same reason, and should be stated.

Please refer to Figures 8 and 9 respectively, which are the comparison diagrams of the influence of the inlet distributor of the present invention on the pressure drop of the refrigerant and the comparison diagram of the influence on the heat transfer coefficient of the refrigerant. In the embodiment, the related performance test and analysis of the plate heat exchanger are mainly based on the experimental method, and the plate heat exchanger 3 of the present invention is installed with the above-mentioned horizontal baffle type inlet distributor (such as the first Figure 1 and Figure 2) Compared with no distributor (shown in Figure 10), the pressure drop (△P _r ) and heat transfer coefficient (W/m) of the refrigerant under different Reynolds number (Re _r ) changes ² ‧℃).

It can be seen from the above experimental results that the horizontal baffle-type inlet distributor installed in the plate heat exchanger is compared with the non-spreader. As the Reynolds number increases, the pressure drop of the refrigerant continues to increase, but the pressure drop of the refrigerant increases. Small, there is not much difference between the two, and the plate heat exchanger is At high flow rates (such as when the Reynolds number is increased from 560 to 860), due to the good mixing of the two-phase liquid and vapor of the fluid, the distribution of the fluid in the plate heat exchanger is more uniform, so the horizontal baffle type inlet distributor is not Compared with the distributor, the heat transfer coefficient is quite close, but at medium and low flow (such as when the Reynolds number is increased from 160 to 560), the plate heat exchanger is installed with a horizontal baffle inlet distributor and no distributor. Compared with the heat transfer coefficient, the heat transfer coefficient is significantly improved, so the fluid can be more evenly distributed in the plate heat exchanger, so that the overall heat transfer performance is better, and the heat exchange efficiency of the plate heat exchanger can be effectively improved.

Therefore, the present invention is mainly aimed at the inlet of the fluid 4 of the plate heat exchanger 3 as the header 1 with an inlet distributor installed, and at least one horizontal baffle 2 is provided on the inner wall of the pipe 11 of the header 1. When the fluid 4 flows into the inlet pipe 32 of the plate heat exchanger 3 through the header 1, the two-phase liquid and vapor of the passing fluid 4 can be separated by the horizontal partition 2 to make the vapor flow along the horizontal The plate surface of the partition plate 2 is guided into the fluid channel 310 at different positions away from the inlet end 321, so as to achieve the purpose of uniform distribution of liquid and vapor mixing at medium and low flow rates, and the pressure drop of the fluid caused by the horizontal partition plate 2 The increase is small, so that the overall heat transfer performance is significantly increased, thereby effectively improving the heat exchange efficiency.

The above detailed description is for a preferred and feasible embodiment of the present invention. However, the embodiment is not intended to limit the scope of the patent application of the present invention. All other equal changes and modifications made without departing from the spirit of the technique disclosed in the present invention All changes shall be included in the scope of patent covered by the present invention.

In summary, the above-mentioned inlet distributor for plate heat exchangers of the present invention can indeed achieve its effects and purposes when used. Therefore, the present invention is truly an invention with excellent practicability, and it meets the requirements of an invention patent. Yan filed an application in accordance with the law and hopes that the review committee will grant the case as soon as possible. In order to protect the inventor's hard work, if there are any doubts, please write to us for instructions, and the inventor will do his best to cooperate with you.

1‧‧‧ Collector

11‧‧‧Pipe

2‧‧‧Horizontal partition

3‧‧‧Plate heat exchanger

31‧‧‧Plate Group

310‧‧‧Fluid channel

311‧‧‧Plate

312‧‧‧First fluid opening

313‧‧‧Second fluid opening

32‧‧‧Inlet pipe

321‧‧‧Entrance

33‧‧‧Export pipeline

331‧‧‧Exit port

34‧‧‧Front Panel

341‧‧‧First fluid interface

342‧‧‧Second fluid interface

35‧‧‧Back Panel

4‧‧‧Fluid

Claims (10)

An inlet distributor for a plate heat exchanger, wherein the plate heat exchanger comprises a plate group arranged face to face at intervals, and a fluid channel is formed between each two adjacent plates of the plate group, and the plate The chip has a plurality of first fluid openings and second fluid openings to form a plurality of inlet pipes and outlet pipes for alternately entering and exiting the fluid channel for heat exchange with more than one fluid, and the inlet distributor includes: a header , Is installed at the inlet end of the inlet pipe, and a pipe for the fluid to pass through is formed inside the header; and at least one horizontal baffle, one end of which is set on the inner wall of the pipe and is separated from the horizontal The other end of the partition plate extends coaxially into the inlet pipe of the plate group, and the horizontal partition plate surface corresponds to the fluid channel, and is used to transfer the two-phase liquid and the fluid passing through the horizontal partition plate. The steam is separated, and the steam is guided along the horizontal baffle to the fluid channel at different positions away from the inlet end. The inlet distributor for a plate heat exchanger described in the first item of the scope of patent application, wherein the inner wall of the header is provided with a plurality of non-equidistantly distributed horizontal partitions in the vertical direction, and the plurality of A horizontal partition divides the pipe to form a plurality of openings of different areas for the fluid to pass through, and the length of each horizontal partition increases sequentially from top to bottom. The inlet distributor for the plate heat exchanger described in the second item of the scope of patent application, wherein the header is provided with two upper and lower horizontal baffles separated by a distance, and between the two horizontal baffles The distance is greater than the maximum distance formed in the vertical direction between the upper horizontal partition and the pipe wall, but smaller than the maximum distance formed in the vertical direction between the lower horizontal partition and the pipe wall. The inlet distributor for the plate heat exchanger described in the first item of the scope of patent application, wherein the inner wall of the header is provided with a plurality of equally spaced horizontal partitions in the vertical direction, and the plurality of The horizontal partition divides the pipeline to form a plurality of openings with different areas for the fluid to pass through, and the length of each horizontal partition increases sequentially from top to bottom. As described in item 4 of the scope of patent application, the inlet distributor for the plate heat exchanger, wherein the header is provided with two upper and lower horizontal baffles separated by a distance, and between the two horizontal baffles The distance is equal to the maximum distance between the upper horizontal partition and the pipe wall in the vertical direction, and the maximum distance between the lower horizontal partition and the pipe wall in the vertical direction. The inlet distributor for a plate heat exchanger described in the first item of the scope of patent application, wherein the length of the horizontal baffle is 1/3 to 2/3 of the total length of the plate group. The inlet distributor for a plate heat exchanger described in the first item of the scope of patent application, wherein the length of the horizontal baffle is 1/3 of the total length of the plate group. The inlet distributor for a plate heat exchanger described in the first item of the scope of patent application, wherein the length of the horizontal baffle is 2/3 of the total length of the plate group. The inlet distributor for a plate heat exchanger described in the first item of the scope of patent application, wherein the horizontal baffle is made of a thin metal material. As described in item 7 of the scope of patent application, the inlet distributor for a plate heat exchanger, wherein the horizontal baffle is made of stainless steel, iron, iron palladium, nickel or nickel-based alloy.

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