Heat exchanger

• US 4,795,618 A
• Filed: 05/23/1986
• Issued: 01/03/1989
• Est. Priority Date: 09/26/1984
• Status: Expired due to Fees

• Current Assignee: M Laumen Thermotechnik GmbH
• Original Assignee: M Laumen Thermotechnik GmbH
• Inventors: Laumen, Michael
• Primary Examiner(s): Hart, Douglas
• Application Number:
  US06/879,128
• Time in Patent Office: 956 Days
• Field of Search: 422/211, 422/222, 422/312, 422/202, 422/198
• US Class Current: 422/202
• CPC Class Codes: B01J 2208/0007 Pressure measurement
• CPC Class Codes: B01J 2208/00256 in a heat exchanger for the heat exchange medium separate from the reactor
• CPC Class Codes: B01J 2208/00309 with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
• CPC Class Codes: B01J 8/0285 Heating or cooling the reactor for tubular reactors in furnaces B01J8/062
• CPC Class Codes: B01J 8/067 Heating or cooling the reactor B01J8/062 takes precedence
• CPC Class Codes: F23C 13/00 Apparatus in which combustion takes place in the presence of catalytic material in a fluidised bed of catalytic particles F23C10/01; radiant gas burners using catalysis for flameless combustion F23D14/18
• CPC Class Codes: F24H 1/0045 with catalytic combustion
• CPC Class Codes: F24H 1/26 the water mantle forming an integral body
• CPC Class Codes: F24H 8/00 Fluid heaters characterised by means for extracting latent heat from flue gases by means of condensation
• CPC Class Codes: F25B 1/08 using vapour under pressure
• CPC Class Codes: F28F 13/003 by using permeable mass, perforated or porous materials F28F13/18 takes precedence
• CPC Class Codes: Y02B 30/00 Energy efficient heating, ventilation or air conditioning [HVAC]

Abstract

A heat exchanger includes a reaction section made of a porous heat-conductive material and a heat transfer section which is connected with the reaction section by a gas-tight highly heat-conductive boundary layer with the heat-conductive material of both sections made preferably of sintered metal; the reaction section sintered metal can be coated with a catalyst substance; fluid medium conduits are provided to pass a heat transfer medium through the heat transfer section while the reaction section is provided with supply and exhaust conduits for a medium to be reacted in the reaction section.

Claims

1. A heat exchanger comprising a reactor section which is connected to supply lines for a flowable composition and through which a flowable composition is passed for effecting a chemical reaction and which comprises a metal structure having a large internal surface comprising a catalytic substance, and

a heat transfer section including at least one gas-tight flow passage for a separate heat transfer fluid of the type having a selected phase transition temperature wherein:

said metal structure comprises porous, sintered metal, said sintered metal being directly heat conductivity joined to a gastight boundary layer which has a high heat transfer coefficient,

the flow passage of said heat transfer section comprising in cross-section, at least in part of its length, porous sintered metal which is directly heat conductively joined to said boundary layer on that side of the reactor section which is opposite to the sintered metal, and

means to conduct said separate heat transfer fluid through said flow passage of said heat transfer section in correlation to the chemical reaction so that the heat transfer fluid will undergo a phase transition at said phase transition temperature thereof in response to said flowable composition undergoing the chemical reaction.

2. A heat exchanger according to claim 1 wherein at least two supply lines for the flowable composition are provided which are spaced apart to supply the flowable composition to different spaced apart regions of the reactor section.

3. A heat exchanger according to claim 1 wherein at least two exit lines for products of the catalytic reaction are provided which are spaced apart to remove products from spaced apart regions of the reactor section.

4. A heat exchanger according to claim 1 wherein a cooler is disposed in the product gas stream leaving the reactor section and is adapted to extract heat from the product gas stream by cooling.

5. The heat exchanger as claimed in claim 4 wherein the cooler is adapted to extract heat from the product gas stream by a condensation of the condensable gases contained in the product gas stream.

6. A heat exchanger according to claims 1, 2 or 3 characterized in that the reactor section (2;

21) comprises at least one flow passage, which is enveloped by the boundary layer (4;

     28) and is particularly disposed in the flow passage of the heat transfer section (3;

     22).

7. A heat exchanger according to claim 1 characterized in that the flow-discharging surface area and flow-receiving surface area of the porous heat-conductive material (5, 10, 23, 29) in the reactor section and/or heat transfer section (2, 3;

21,

     22) exceeds to the cross-sectional area of the flow passage of the reactor section and/or the heat transfer section (2;

     21), respectively, and in particular is oblique.

8. A heat exchanger according to claim 1, characterized in that the flow passages of the reactor section and of the heat transfer section (2, 3;

21,

     22) comprise a downstream portion in which a smaller part of the cross-sectional area of the flow passages is filled with solid particles (11) of the porous heat-conductive material than in an upstream portion.

9. A heat exchanger according to claim 8, characterized in that the proportion in which the cross-sectional area of the flow passages is filled with solid particles (11) of the porous heat-conductive material decreases in the direction of flow continuously.

10. A heat exchanger according to claim 8 or 9, characterized in that the porous heat-conductive material in the reactor section and in the vapor-generating section (2, 3;

21,

     22) consists of a block (5, 10, 6;

23, 24,

     29), in which the solid particles are less densely packed in the downstream portion than in the upstream portion.

11. A heat exchanger according to claim 8 or 9, characterized in that the blocks (5, 10, 6;

23, 24,

     29) of the reactor section the heat transfer section (2, 3;

21,

     22) are composed of a plurality of block segments (24, 24a, 24b, 29a, 29b, 29c).

12. A heat exchanger according to claim 8 or 9 characterized in that the boundary layer (4;

28) of the flow passages of the reactor section and the heat transfer section (2, 3;

21,

     22) is clear of the porous heat-conductive material (5, 10, 6;

23, 29, 29a) in the entrance portion of the flow passages.

13. A heat exchanger according to claim 1 characterized in that the porous heat-conductive material (5, 10;

23) in that portion of the reactor section (2;

     21) which is the upstream portion in the flow of the educts (8;

     27) serves to preheat the flowable composition and the flowable composition.

14. A heat exchanger according to claim 4, characterized in that the cooler (37) includes sintered metal.

15. A heat exchanger according to claim 14, characterized in that the reactor bed (24) and the cooler (37) are thermally separated from each other by a spacing section (38).

16. A heat exchanger according to claim 4, characterized in that the cooler (37) comprises an evaporator (36) of a heat pump circuit.