Device for compressing and drying gas

Patent metadata

Field	Value
Publication number	US-9050554-B2
Application number	US-201113697203-A
Country	US
Kind code	B2
Filing date	May 11, 2011
Priority date	May 11, 2010
Publication date	Jun 9, 2015
Grant date	Jun 9, 2015

Abstract

Device for compressing and drying gas includes a multistage compressor with a low pressure stage, a high pressure stage, and a pressure pipe; and an adsorption dryer with a drying zone and a regeneration zone. An intercooler is located between the low pressure stage and high pressure stage, and the device includes a heat exchanger with a main compartment with an inlet part and an outlet part for a first primary fluid. The ends of the tubes of the heat exchanger are connected to a separate inlet compartment and outlet compartment for each series of tubes. A first series of tubes forms a cooling circuit of the intercooler in order to heat up gas from the high pressure stage for the regeneration of the adsorption dryer.

First claim

The invention claimed is:

1. A device for compressing and drying gas, comprising:
a multistage compressor having a low pressure stage, a high pressure stage with a pressure pipe and an adsorption dryer with a drying zone and a regeneration zone;
an intercooler located between the low pressure stage and high pressure stage,
a heat exchanger connected to an inlet part by the pressure pipe,
the heat exchanger including a housing with a number of compartments, including a main compartment with said inlet part and an outlet part for a first primary fluid that is guided in the main compartment over or around tubes that extend through the main compartment;
at least two series of tubes that extend through the main compartment, and which are each configured to guide a secondary or tertiary fluid through the main compartment to exchange heat with the primary fluid;
the ends of the tubes being connected respectively to a separate inlet compartment and outlet compartment for each series of tubes;
a first of said series of tubes forming a first cooling circuit of the intercooler,
a second of said series of tubes forming a second cooling circuit of the said heat exchanger;
the inlet compartment of said second series of tubes being directly connected via a branch pipe to an outlet pipe of said high pressure stage; and
the outlet compartment of said second series of tubes being connected to said regeneration zone of said adsorption dryer and arranged to heat gas coming from the high pressure stage for the regeneration of the adsorption dryer.

2. The device according to claim 1 , wherein the main compartment comprises a number of inlet and outlet parts for a number of primary fluids.

3. The device according to claim 1 , wherein the main compartment is bounded by two end plates and on either side of the main compartment a cover forms two side compartments between each respective end plate and a cover opposite it.

4. The device according to claim 3 , wherein the tubes are fastened in one of the end plates.

5. The device according to claim 3 , wherein the side compartments include the inlet and outlet compartments.

6. The device according to claim 5 , wherein the side compartments are subdivided into two or more sub-compartments and the respective sub-compartments are connected on either side of the main compartment by the series of tubes such that at least two separate circuits for at least the respective secondary and tertiary fluid are formed.

7. The device according to claim 1 , wherein the main compartment includes baffles, for the primary fluid.

8. The device according to claim 3 , wherein the heat exchanger includes two or more extra fluids and the respective side compartments are subdivided on either side of the main compartment by partitions in the inlet and outlet compartments, including a first inlet and outlet compartment that connects to a first group of tubes and guides a secondary fluid and a second inlet and outlet compartment connecting a second group of tubes guiding a tertiary fluid.

9. The device according to claim 8 , wherein a seal is provided between the partitions and end plates.

10. The device according to claim 8 , wherein a space is provided between the first group and second group of tubes.

11. The device according to claim 8 , wherein the tubes of the first and second group are distributed over a sector of a circle.

12. The device according to claim 8 , wherein the tubes are distributed in a concentric arrangement, so that the first group of tubes is located within a circle and the second group of tubes is located in a ring around said circle.

13. The device according to claim 1 , wherein the inlet and outlet part of the heat exchanger are located on a side of a shell that borders the main compartment.

14. The device according to claim 8 , wherein the first inlet and the first outlet compartment are located on an opposite side of the heat exchanger, while the second inlet and outlet compartment are located on the same side of the heat exchanger.

Assignees

• Janssens Stijn Jozef Rita Johanna
• Pahner Uwe
• Briers Christophe
• Atlas Copco Airpower Nv

Inventors

• Janssens Stijn Jozef Rita Johanna
• Pahner Uwe
• Briers Christophe

Classifications

• F28F9/22

  Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates · CPC title

• F28D7/0091

  the supplementary medium flowing in series through the units · CPC title

• F28D7/0083

  with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium · CPC title

• B01D2259/4009

  using hot gas · CPC title

• F28D7/1607

  with particular pattern of flow of the heat exchange media, e.g. change of flow direction (F28D7/1623, F28D7/1638, F28D7/1661, F28D7/1676, F28D7/1692 take precedence) · CPC title