FLUID-TREATMENT COLUMN WITH PARTITION

Abstract

A column for performing thermal separation processes and/or chemical reactions has a vertical outer wall that forms a chamber and a vertical partition subdividing the chamber into two compartments. The partition being formed by flat plates each being made of or covered by heat-insulating material.

Claims

1. A column for performing thermal separation processes and/or chemical reactions, the column comprising: a vertical outer wall that forms a chamber; and a vertical partition subdividing the chamber into two compartments, the partition being formed by flat plates each being made of or covered by heat-insulating material.

2. The column defined in claim 1, wherein the plates have opposite side faces at least one of which is clad with the heat-insulating material.

3. The column defined in claim 1, wherein the plates are at least partly made of plastic or ceramic.

4. The column defined in claim 1, wherein the plates are made of plasmic with carbon fibers for reinforcement.

5. The column defined in claim 1, wherein the plates are at least partly made of polytetrafluoroethylene.

6. The column defined in claim 1, further comprising: screw connectors interconnecting the plates.

7. The column defined in claim 1, further comprising: plug connectors interconnecting the plates.

8. The column defined in claim 1, wherein the plates are clad with metallic elements.

9. The column defined in claim 1, further comprising: at least one mass-transfer pack in one of the compartments.

Description

BRIEF DESCRIPTION OF THE DRAWING

[0010] The above and other objects, features, and advantages will become more readily apparent from the following description, reference being made to the accompanying drawing in whose sole FIGURE a column partition is shown in section.

SPECIFIC DESCRIPTION OF THE INVENTION

[0011] An unillustrated cylindrical column with a vertical cylindrical axis has a schematically illustrated cylindrical outer wall made of sheet metal of which two parts are illustrated not to scale at 10. It is internally divided by at least one generally planar and vertical partition 1 into two compartments 2 and 3 in which mass-transfer packs such as illustrated schematically at 11 are provided that ensure that thermal separation processes and/or chemical reactions occur between a liquid that is flowing in from above and a gas that is flowing in from below. In the embodiment shown in the drawing, the partition 1 is formed by sheet-metal plates 4 that are one above the other and can be welded together at the edges.

[0012] On one side, the supporting plates 4 are provided with a one-sided cladding 5 formed by tiles 5a and 5b that are made of a heat-insulating material, particularly plastic (for example PTFE) and/or ceramic, preferably with carbon fibers for reinforcement. Threaded pins 6 projecting laterally from the tiles 5a and 5b, extend through holes 7 in the plates 4, and carry nuts 8 on their free ends. A vertical brace plate 9 can be provided between the nuts and the plates 4.

[0013] Alternatively, the plates 4 themselves are made of heat-insulating material(s) and, furthermore, the plates can be connected to one another by plug connectors. Additional protection of the plates is achieved if the plates are encased in metal.

[0014] A specific embodiment of an insulated partition is described below:

[0015] In the case of a partition 1 made of stainless steel plates 4 with a thickness of 1.5 mm, heat transfer of 592 kW occurs between the two sides of the partition. If insulation cladding 5 of 5 mm thick PTFE is applied to this 1.5 mm-thick stainless steel sheet 4, the heat transfer drops to 14.4 kW. This corresponds to a reduction of 97.5%. It is crucial that the heat conduction of stainless steel be 15 W/(m K) and that the heat conduction of PTFE be 0.25 W/(m K). This observation applies to the assumption that steam is primarily responsible for the heat transfer on both side faces of the partition. Therefore, the heat transfer coefficient of the gas phases is assumed to be 5000 W/(m.sup.2 K). Assuming that liquid is responsible for the transferred heat on both side faces of the partition, and in expectation of a heat transfer coefficient of 500 W/(m.sup.2 K), heat flux of 72 kW occurs without isolation and 12.2 kW with insulation. This still corresponds to a savings of 83.1%.