RU73062U1 - PLATE HEAT EXCHANGER PLATE - Google Patents

Abstract

The utility model relates to elements of plate heat exchangers through which heat is exchanged between two media (liquids or steam and liquid). Technical results: equalization of the hydrodynamic parameters of the elementary volumes of the cooled or heated liquid along the width of the plate when they approach from the inlet through the distribution-collector part to the main heat exchange part and increase the efficiency of heat transfer between the two media. The plate heat exchanger plate includes a main heat exchange part, distribution and collector parts, holes for providing the influx and outflow of a cooled or heated liquid or steam, corrugation: for the location of sealing gaskets, heat exchange part, near the holes, distribution and collector parts, and the edges of the corrugations near the holes, opposite holes, are made with a variable canopy, providing different hydrodynamic resistance at the inlet.

Description

Technical field

The utility model relates to elements of plate heat exchangers through which heat is exchanged between two fluids (liquids or steam and liquid), which are assembled together with sealing gaskets in a unit designed to separate the heated and cooled fluids, which are located on both sides of the plate.

State of the art

An analogue of the proposed plate can be considered the product described in US patent No. 4678030, which was published on 07/07/1987, IPC F28D 9/00. The analogue contains the main heat exchange part located between the two distribution-collector parts, holes located in the corner parts of the distribution-collector parts, corrugations for the location of sealing gaskets, corrugation of the heat exchange part, corrugation of the distribution-collector parts, corrugation near the holes.

The disadvantages of the analogue are: insufficiently aligned hydrodynamic parameters of the elementary volumes of the cooled or heated liquid along the width of the plate when they approach from the inlet through the distribution-collector part to the main heat exchange part, as a result, the heat exchange between honey and two media is not high enough.

The closest analogue for the proposed plate can be considered the plate described in the patent of the Russian Federation No. 2113030, which was published on 04/27/1998, IPC F28D 9/00, including the main heat exchange part located between the two distribution-collector parts, openings located in the corner parts distribution-collector parts, corrugations for the location of sealing gaskets, corrugation of the heat exchange part,

corrugation of distribution-collector parts, corrugation near holes.

The disadvantages of the closest analogue are: insufficiently aligned hydrodynamic parameters of the elementary volumes of the cooled or heated liquid along the width of the plate when they approach from the inlet through the distribution-collector part to the main heat exchange part, as a result - the heat exchange between honey and two media is not high enough.

Utility Model Disclosure

Traditionally manufactured plates for plate heat exchangers usually have corrugations of the distribution-collector parts that do not provide different hydrodynamic resistance. Such plates, assembled together with sealing gaskets in a heat exchanger, provide insufficiently high efficiency of heat transfer between two media in connection with insufficiently aligned hydrodynamic parameters of elementary volumes of cooled or heated liquid along the width of the plate when they approach from the inlet through the distribution-collector part to the main heat-exchange part. In such initial conditions, the movement of elementary volumes of cooled or heated liquid along the main heat exchange part occurs with equalization of hydrodynamic parameters, depending on the flow rate and pressure in various plate heat exchangers from 1/3 to 1/2 of the plate length, which can be observed when analyzing deposits on the plates who have worked in heat exchangers for quite a long time. The analysis of deposits on such plates shows a higher intensity of deposits in the zone of the main heat exchange part from the inlet side and lower intensity from the opposite side. Closer to the outlet, the sediment intensity is leveled off. The unevenness of the intensity of deposits shows insufficiently high efficiency

the use of the main heat exchange part of the analogues of the proposed plate.

The objective of the utility model is to increase the efficiency of heat transfer between two media.

Technical results of the utility model: alignment of the hydrodynamic parameters of the elementary volumes of the cooled or heated liquid along the width of the plate when they approach from the inlet through the distribution-collector part to the main heat exchange part and increase the efficiency of heat exchange between honey in two media.

Technical results are achieved in that the plate heat exchanger plate, assembled together with the sealing gaskets in the block, includes a main heat exchange part located between the two distribution-collector parts, and openings located in the corner parts of the distribution-collector parts, to ensure the inflow and outflow of the cooled or heated liquid or steam, corrugation for the location of sealing gaskets, corrugation of the heat exchange part, corrugation near the holes, corrugation distribution separating collector parts, the edges of the latter being made with a variable canopy - decreasing from the region of the smallest path from the inlet to the main heat exchange part to the region of the largest path from the inlet to the main heat exchange part, providing different hydrodynamic resistance with its increased value in the region of the smallest path from the inlet to the main heat exchange part and its reduced value in the region of the largest path from the inlet to the main heat exchange part and with the alignment of the parameters of the elementary volumes of the cooled or heated liquid when they approach from the inlet through the distribution-collector part to the main heat-exchange part. The edges of the corrugations near the holes, opposite the holes, can be made with a variable cavity both in profile and in plan.

Brief Description of the Drawings

Figure 1 presents a diagram of a plate plate heat exchanger. Figure 2 presents the diagram of the corrugation of the distribution-collector parts, which are made with a variable cavity.

Utility Model Implementation

The plate heat exchanger plate, assembled together with sealing gaskets in the block, includes a main heat exchange part 1 located between two distribution-collector parts 2 and 3, and openings 4, 5, 6, and 7 located in the corner parts 8, 9, 10, and 11 distribution-collector parts, respectively, corrugation for the location of the sealing gaskets 12, corrugation of the heat exchange part 13, corrugation of the distribution-collector parts 14 and 15, corrugation near the holes 16.

The plate plate heat exchanger operates as follows. The elementary volumes of liquid moving from the hole 4 along the plate receive greater resistance to movement in the region of the smallest path from the hole 4 to the main heat exchange part 1 and less in the region of the greatest path from the hole 4 to the main heat exchange part 1. This ensures equalization of the hydrodynamic parameters of the elementary volumes liquid when they approach from the hole 4 through the distribution-collector part 2 to the main heat exchange part 1.

The manufacture of a plate for plate heat exchangers can be carried out from known materials, for example, from metals by known methods, for example, by stamping.

Claims (3)

1. Plate heat exchanger plate, including the main heat exchange part located between the two distribution-collector parts, and holes located in the corner parts of the distribution-collector parts, to ensure the inflow and outflow of cooled or heated liquid or steam, corrugation for the location of sealing gaskets, corrugation heat exchange parts, corrugation of distribution-collector parts, corrugation near holes, assembled together with sealing gaskets in a block, excellent in that the corrugation edges of the distribution and collector parts are made with a variable cavity - decreasing from the region of the smallest path from the inlet to the main heat exchange part to the region of the largest path from the inlet to the main heat exchange part, providing different hydrodynamic resistance with its increased value in the region of the smallest the path from the inlet to the main heat exchange part and its reduced value in the region of the largest path from the inlet to the main heat exchange part with alignment of the parameters of the elementary volumes of the cooled or heated liquid when they approach from the inlet through the distribution-collector part to the main heat exchange part. 2. The plate according to claim 1, characterized in that the corrugation of the distribution-collector parts is made with a variable canopy in plan. 3. The plate according to claim 1, characterized in that the corrugation of the distribution-collector parts is made with a variable cavity in the profile.