Priority is claimed to Italian application MI2001A 002034, filed Oct. 1, 2001, which is incorporated by reference herein.
The present invention relates to a device used as a chemical reactor or heat exchanger in general, with a thin tube plate. The present invention also applies to petrochemical and refinery reactors.
Chemical reactors generally consist of large-sized containers inside of which chemical reactions take place at a high temperature and high pressure. The substantially cylindrical body of the chemical reactors generally have a plurality of pipes or tube bundles which carry out various functions, such exchanging heat between two or more operating fluids. These tube bundles are installed and retained in their operative position by tube plates, which in some cases have a large surface area.
Conventional tube plates are produced in a single piece or in several welded pieces. The plates are then finished by drilling or machining. The tube plates are usually designed with a sufficient thickness to withstand the loads expected to be applied to the plates and reactors.
The loads applied to the tube plates may be due to weight, pressure and/or temperatures in an operating chemical reactor. The loads can generate high levels of stresses in the plates. To withstand these stresses, the plates have been made relatively thick. But a thick tube plate may be technically unfeasible in some applications. Where a thin tube plate is needed, then the plates can be thinned and supported with added strength enhancing elements. Various methods for strengthening tube plates are known according to the state of the art. Design codes are also known which regulate the dimensional criteria for the plates and for strengthening the latter.
In general the known tube plate strengtheners consist of reinforcement ribs, which are welded to the thin plates such as to limit the deformations and stresses to which the plates are subjected. These strengtheners are costly and their size, by reducing considerably the useful space for insertion of the tubes on the plates, leads to a significant increase in the diameter of the plates themselves and consequently in the overall diameter of the equipment.
In one embodiment, the present invention eliminates the aforementioned disadvantages and in particular to provide a device which is used as a chemical reactor or heat exchanger in general, with a thin tube plate, which makes it possible to reduce the costs of construction of the device itself. This embodiment provides a device which is used as a chemical reactor or heat exchanger in general. The embodiment includes a thin tube plate which lightens the device and facilitates its installation.
The embodiment also provides a thin tube plate device for use as a chemical reactor or heat exchanger which is safe and reliable when installed. The embodiment further provides a device for use as a chemical reactor or heat exchanger in general with a thin tube plate which is simple and functional.
The characteristics and advantages of a device used as a chemical reactor or heat exchanger having a thin tube plate according to the present invention will become clearer and more apparent from the following description provided by way of the non-limiting example with reference to the attached schematic drawings, in which:
A chamber 116 which acts as a fluid distributor is connected to the tube plate 114. The chamber 116 may be produced in the shape of a āUā. The chamber 116 includes a base 118 joined to the plate 114 by a cylindrical or lateral section 120, with generatrices parallel to the axis of the pipes.
The plate 114 of the device 110 is connected at the base 118 of the chamber 116 both by means of the cylindrical portion 120 and by means of connection elements 122 which are disposed inside the cylindrical portion 120. These connection elements 122 are cylindrical or flat portions with a shape similar to the lateral portion 120. The example shows one of these elements 122, disposed axially symmetrically relative to the axis of the pipe 112, although other configurations can be used.
The functioning of the device 110 used as a chemical reactor or heat exchanger in general, is apparent from the foregoing description provided with reference to the figures. In the case of the known art, the loads are transmitted entirely by the device 10 through the plate 14 to the cylindrical portion 20 of the chamber 16. In the device 110 shown in
The description provided makes apparent the characteristics of the device used as a chemical reactor or heat exchanger in general, with a thin tube plate, as well as certain corresponding advantages including:
The invention can be applied to chemical reactors, petrochemical reactors, refinery reactors, heat exchangers, and in general to tube bundle-type pressure devices.
While the invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not to be limited to the disclosed embodiment, but on the contrary, is intended to cover body, and the coil winding having side sections adjacent the flat surfaces.
Number | Date | Country | Kind |
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MI2001A2034 | Oct 2001 | IT | national |
Number | Name | Date | Kind |
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4337224 | Mahler et al. | Jun 1982 | A |
5266281 | Kao et al. | Nov 1993 | A |
Number | Date | Country | |
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20030086843 A1 | May 2003 | US |