Heat exchange system

Patent metadata

Field	Value
Publication number	US-9568251-B2
Application number	US-201214116662-A
Country	US
Kind code	B2
Filing date	Apr 17, 2012
Priority date	May 11, 2011
Publication date	Feb 14, 2017
Grant date	Feb 14, 2017

Abstract

The present invention relates to a heat exchange system comprising:—a single apparatus (N) having an area immersed in a fluid bath (N 2 ) and a free space (N 1 ) at the head in which a vapour phase is accumulated,—at least one interspace (P) open at both ends, situated inside said apparatus and completely immersed in the fluid bath,—one or more heat exchange surface (s) ( 6, 7, 8, 9, 10, 11 ), said system characterized in that it contains all the heat exchange surfaces in a single apparatus and said surfaces are completely immersed in the fluid bath and are fluidly connected to the hot and cold sources, external to said system, through flows of matter. At least one of the heat exchange surfaces ( 6, 7, 8 ) is situated inside the interspace and at least another surface ( 9, 10, 11 ) is situated in the space between said interspace and the walls of the apparatus.

First claim

The invention claimed is:

1. A heat exchange system comprising:
a single apparatus having an area immersed in a fluid bath and a free space at the apparatus head in which a vapour phase is accumulated,
at least one interspace open at both ends, situated inside said apparatus and completely immersed in the fluid bath,
one or more heat exchange surface(s) which yield heat to one or more flows of cold material,
one or more heat exchange surface(s) which absorb heat from one or more flows of hot material,
at least an inlet gate for the one or more flows of cold material coming from an external cold source and at least an inlet gate for the one or more flows of hot material coming from an external hot source,
at least an outlet gate for at least a flow of cooled material and at least an outlet gate for at least a flow of heated material by means of said heat exchange surfaces,
wherein:
said system contains all the heat exchange surfaces in the single apparatus,
said heat exchange surfaces are completely immersed in the fluid bath and are fluidly connected to the hot and cold sources, external to said system, through flows of material,
the heat exchange surface(s) which yield heat to the one or more flows of cold material are situated inside the interspace and the heat exchange surface(s) which absorb heat from the one or more flows of hot material are situated in the space between said interspace and the walls of the apparatus, and
the external hot sources and the cold sources are hot material and cold material generated in the production process of hydrogen or synthesis gas, or both.

2. The heat exchange system according to claim 1 , which also comprises at least one steam turbine coupled with at least one electric generator.

3. The heat exchange system according to claim 1 , wherein the heat exchange surfaces are in the form of helicoidal elements in which the streams of material flow.

4. The heat exchange system according to claim 3 , wherein there are at least six helicoidal elements.

5. The heat exchange system according to claim 1 , wherein the interspace is cylindrically shaped.

6. The heat exchange system according to claim 1 , wherein the fluid is water and the vapour phase is steam.

7. The heat exchange system according to claim 1 , wherein there are at least three inlet gates for the flow of cold material, and at least three inlet gates for the flow of hot material.

8. The heat exchange system according to claim 1 , wherein there are at least six heat exchange surfaces.

9. The heat exchange system according to claim 1 , wherein the flows of cold material are at least one of reagents, oxidants or inert products coming from a catalytic partial oxidation process.

10. The heat exchange system according to claim 1 , wherein the flows of hot material are products coming from at least one of a catalytic partial oxidation reaction step, a Water Gas Shift step or a combustion step of a catalytic partial oxidation process.

11. A heat exchange and recovery process that uses the heat exchange system according to claim 1 , comprising the following phases:
cooling a flow of material coming from the external hot source, in said heat exchange system, by means of water,
heating a flow of material coming from the external cold source, in said heat exchange system, by means of steam, and
transforming the excess heat present in said heat exchange system into steam.

12. The heat exchange and recovery process according to claim 11 , wherein the heat exchange surfaces inside the interspace, included in the heat exchange system, transfer heat to the flows of cold material, heating them, and the heat exchange surfaces between the interspace and walls of the apparatus absorb heat from the flows of hot material, cooling them.

13. The heat exchange and recovery process according to claim 12 , wherein the steam generated is fed to a steam supply system or used for generating electric energy.

14. The heat exchange and recovery process according to claim 12 , wherein the flows of heated material enter a desulfuration or catalytic partial oxidation reaction steps of a catalytic partial oxidation process, or both.

15. The heat exchange and recovery process according to claim 12 , wherein the flows of cooled material enter at least one of a water gas shift step, a hydrogen separation or purification step of a catalytic partial oxidation process.

Assignees

• Basini Luca Eugenio
• Wilhelm Alfred Joachim
• Eni Spa

Inventors

• Basini Luca Eugenio
• Wilhelm Alfred Joachim

Classifications

• F28D15/00 Primary

  Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls {; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies (F28D17/00, F28D19/00, F28D20/00 take precedence)} · CPC title

• C01B3/386

  Catalytic partial combustion · CPC title

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title

• C01B2203/0883

  by indirect heat exchange · CPC title

• C01B2203/0894

  Generation of steam · CPC title