US3892499A - Multistage turbocompressor having an intermediate cooler - Google Patents
Multistage turbocompressor having an intermediate cooler Download PDFInfo
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- US3892499A US3892499A US378428A US37842873A US3892499A US 3892499 A US3892499 A US 3892499A US 378428 A US378428 A US 378428A US 37842873 A US37842873 A US 37842873A US 3892499 A US3892499 A US 3892499A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/58—Cooling; Heating; Diminishing heat transfer
- F04D29/582—Cooling; Heating; Diminishing heat transfer specially adapted for elastic fluid pumps
- F04D29/5826—Cooling at least part of the working fluid in a heat exchanger
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D17/00—Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
- F04D17/02—Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps having non-centrifugal stages, e.g. centripetal
- F04D17/025—Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps having non-centrifugal stages, e.g. centripetal comprising axial flow and radial flow stages
Definitions
- multistage turbocompressors have been known to use an intermediate cooler between various compressors in order to cool a gaseous working medium, e.g. steam, flowing between the compressors.
- a gaseous working medium e.g. steam
- the gaseous working medium may cool to such an extent, either temporarily or for a relatively long time, as to allow the water vapor therein to begin to condense. Should this occur, the condensed water vapor would be delivered as water droplets to the blading channels of the turbocompressor and would cause damage through erosion and depositing of impurities contained in the gas flow.
- Axial blading is particularly endangered because higher speeds of the working medium to be compressed are generated relative to the blade surfaces driving the medium than is the case with the blading of a radial compressor.
- the invention provides a multistage turbocompressor comprised of a compressor housing and an intermediate cooler outside the housing with a casing duct between the housing and cooler and a central duct enclosed within the casing duct and between the cooler and housing.
- the casing duct is connected to pass a flow of heated compressed gas from the housing, for example, from an initial compressor therein, to the cooler for cooling to suitable temperature for subsequent use.
- the central duct is connected to pass the flow of cooled compressed gas back to the housing, for example, to a second compressor.
- the heated gas heats the wall of the central duct.
- the resultant heat in the wall of the central duct then heats any condensate in the countercurrent flow of cooled gas within the central duct to vaporize the condensate.
- the return flow of gas becomes free of condensate.
- Gas turbine equipment such as described in Swiss Pat. Nos. 2 l4,837 and 22 l ,377 have been known to use piping systems with a central duct disposed within a casing duct.
- these piping systems have been used to conduct a high-temperature gas through the central duct.
- a cooler gas has been conducted in the outer casing duct. ln this way, it has been possible to obtain thermal relief of the wall loaded by the high internal pressure, avoiding strength problems and leak-proofing difficulties.
- the hot gas is conducted in the outer casing duct and the cool gas in the central duct.
- the tube wall dividing the casing duct from the central duct can be maintained at a hightemperature by means of the flow of not-yet-cooled gas.
- the flow of cool gas laden with drops of condensate is surrounded on all sides by a hightemperature wall.
- the drops become 2 vaporized before reaching the blading of the compres' sor.
- the compressor may have an axial stage upstream of the exit point to the cooler of the medium being compressed, and may have a radial stage following the reentry of the cooler medium.
- the invention is of special importance for compressors with use axial stages following the re-entry of the cooled medium.
- the function of the casing duct can be substantially facilitated by forming a bend in the casing duct as well as in the central duct since the drops of condensate will impact against the wall, and produce a greater surface area of contact. Thus revaporization can be accelerated.
- the casing duct and central duct can advantageously be connected to the lower half of the housing where the housing is split in two halves. Also, it is possible to have two casing ducts disposed symmetrically of the perpendicular axial plane of the turborotor with each connected to the housing. Finally, a means may be disposed between the casing duct and the central duct to selectively introduce a variable amount of heated gas from the casing duct into the flow of cooled gas in the central duct in order to further promote the vaporization of the condensate drops.
- FIG. 1 illustrates an axial cross-sectional view of a turbocompressor according to the invention
- FIG. 2 illustrates a cross-sectional view taken on the plane llll of FIG. 1.
- FIG. 3 illustrates an axial cross-sectional view of a further turbocompressor construction according to the invention made as a purely axial compressor
- FIG. 4 illustrates a cross-sectional view through a compressor with separate intermediate coolers disposed at both sides according to the invention.
- an axial-radial turbocompressor includes in a housing 1 in which a rotor 2 is mounted and which has an inlet A for receiving air or a gas.
- the rotor 2 carries axial rotor rings 3 to 10 to compress air or a gas to a pressure at which the temperature rises to such an extent that intermediate cooling is necessary.
- the rotor 2 also carries radial stages ll and 12 of a radial compressor to compress the gas further to a final pressure after cooling.
- the housing I also has an outlet B at the end of the radial compressor for the exhaust of the compressed gas.
- a casing duct 13 is connected to the housing 1 between the axial stages 3 to 10 and the radial stages 11, 12 (FIG. 1) and extends to a cooler 14 (FIG. 2) to conduct the flow of heated compressed gas to the cooler 14.
- a central duct 15 is enclosed within the casing duct 13 and extends from the cooler 14 to the housing 1 to conduct the flow of cooled compressed gas back to the housing and to the radial stages ll, 12.
- both ducts l3, 15 have a curved or bent position to deflect the respective flows of gas for purposes as described below.
- the gas may be cooled in the intermediate cooler 14 to such an extent that the water contained in the gas before compression (or some other condens able inclusion) becomes condensed into drops.
- These drops are carried along by the gas flowing back into the compressor, and would, without an introduction of heat, only revaporize during the compression in the radial stage 11, and deposit non-vaporized impurities on the blade surfaces. Non-vaporized residues might even arrive in stage 12.
- erosion and premature wear of these parts may occur.
- the wall of the central duct 15 is supplied with heat from the gas heated through compression in stages 3 to and flowing into the casing duct 13.
- the drops of liquid carried along by the cooled gas receive so much heat that they revaporize and, as vapor, can no longer cause damage to the radial rotors 11 and 12.
- the solid constituents are now dry, and are forced through the compressor without becoming deposited on the blades.
- the vaporization of the drops of liquid in the central duct 15 can occur, in part, in the suspended state through the radiation of heat from the wall and also, in part, through contact with the duct wall. Because of the turbulence of the gas and the curved portions of the duct 15 some of the drops strike the heated duct wall and thereby become broken up. This gives the drops an enlarged surface area, thereby promoting more rapid vaporization. If there is a danger of a particularly great formation of liquid drops, then it is possible to install guide elements in the central duct to separate the drops out of the gas flow and conduct the drops against the wall. Such guide elements could also aid in the vaporization of the drops of condensate if heated to a suff' cient temperature by radiation from the duct walls.
- an axial compressor having axial stages 16 to 21 follow the intermediate cooler (not shown).
- Axial stages are more endangered by drops in the gaseous working medium being com pressed and by deposits than are radial stages, and in their flow, undergo greater deviations than radial compressors.
- the most endangered parts are the blades of the introduction-stator 22 first reached by the intermediately cooled gas. These blades do not receive the flow of gas from the central duct 15 as uniformly as do the blades of the following rotors 16 to 21 and stators 23 to 28.
- aa turbocompressor can be provided at each side of the housing 1 with an intermediate cooler 14.
- the housing 1 is split into two halves. with the connection of each cooler 14 made in the lower housing half 29 by flanges 30. This facilitates access to the rotor 2 for maintenance and overhauling work.
- a means 31-33 is also provided between the casing duct 13 and the central duct 15 in order to selectively introduce a small variable amount of not-yetcooled medium being compressed from the casing duct 13 into the central duct 15.
- This means includes a pipe 31 connecting the casing duct 13 to the central duct 15, a series of outlets 32 in the pipe 31 to introduce the heated gas into the central duct 15 and a valve 33 for controlling the amount of flow through the pipe 31. This conducts so much heat to the cool gas in the central duct 15, which still contains drops, that any drops not reaching the wall and not sufficiently heat-irradiated by the wall become vaporized. An undesirable reheating of the cooled gas is not to be expected because the brought-in heat is used chiefly to vaporize the drops.
- a multistage turbocompressor having a compressor housing including an inlet and an outlet and an intermediate cooler outside said housing;
- a casing duct connected between said housing and said cooler downstream of said inlet for passing a flow of heated compressed gas from said housing to said cooler for cooling therein,
- a central duct enclosed within said casing duct and connected between said cooler and said housing upstream of said outlet for passing the flow of cooled compressed gas from said cooler to said housing for passage out of said outlet.
- a multistage turbocompressor comprising a housing including an inlet and an outlet;
- a first compressor in said housing downstream of said inlet for heating and compressing a flow of gas to a first pressure
- a second compressor in said housing downstream of said first compressor and upstream of said outlet for compressing the flow of gas to a higher pressure than said first pressure
- a cooler outside said housing for cooling the flow of heated gas
- a central duct enclosed within said casing duct and connected between said cooler and said housing for passing the flow of cooled gas from said cooler to said second compressor.
- each duct has a bend therein for deflecting a respective flow of gas therein.
- a multistage turbocompressor as set forth in claim 6 further comprising a means connected between said casing duct and said central duct for selectively introducing a variable amount of heated gas from said 6 casing duct into the flow of cooled gas in said central to said cooler, duct. a central duct concentric to said casing duct and conll.
- a multistage turbocompressor comprising nected between said cooler and said housing for a compressor housing having an inlet and an outlet, passing the flow of cooled gas from said cooler to a first plurality of compressor stages in said housing 5 said housing downstream of said compressor adjacent and downstream of said inlet to receive stages.
- a second plurality of compressor stages in said housa cooler outside said housing for cooling the flow of ing downstream of said first compressor stages and compressed gas, upstream of said outlet for compressing the flow of a casing duct connected between said housing and 10 gas from said cooler and central duct.
- said cooler for passing the flow of compressed gas
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- Structures Of Non-Positive Displacement Pumps (AREA)
Abstract
The compressor housing is connected to the cooler by a casing duct to direct the intially compressed gas to the cooler while a central duct within the casing duct returns the cooled air to the housing and to the second compressor. The heated wall of the central duct serves to vaporize any droplets of fluid in the return gas flow which might otherwise damage the second compressor.
Description
Strub July 1, 1975 [54] MULTISTAGE TURBOCOMPRESSOR 2,540,99l 2/l95l Price 4l5/l79 HAVING AN INTERMEDIATE COOLER f; z' a [75] Inventor: Rene Strub, Winterthur, Switzerland 2,925,954 2 9 0 Spillmann et a1. 4|5 |79 Assignee: Sulzer Brohers wintenhurv $195,458 3/1974 Strub .7 4l5/l79 S 't l d w! zer an Primary Examiner-C. J. Husar Filedi 1973 Attorney, Agent, or Firm-Kenyon & Kenyon Reilly 2 l] Appl. No: 378,428 & Chapn [30] Foreign Application Priority Data [57] ABSTRACT July 13 [972 switzjfland l0517/72 The compressor housing is connected to the cooler by a casing duct to direct the intially compressed gas to 52 s Cl. U 4 5 179. 415 417 372 the COOlCl' while a central dUCt within I116 casing duct 5 I] Im. cI. .1 Eula 5/08 mums the to the housing and sewnd [58] new of Search H 7/372. 415/179 168 compressor. The heated wall of the central duct serves to vaporize any droplets of fluid in the return gas flow [56] References Cited which might otherwise damage the second compres- UNITED STATES PATENTS 2.396.484 3/!946 Allen et al. 415/179 11 Claims, 4 Drawing Figures MULTISTAGE TURBOCOMPRESSOR HAVING AN INTERMEDIATE COOLER This invention relates to a multistage turbocompressor having an intermediate cooler.
Heretofore, multistage turbocompressors have been known to use an intermediate cooler between various compressors in order to cool a gaseous working medium, e.g. steam, flowing between the compressors. However, a danger has existed that the gaseous working medium may cool to such an extent, either temporarily or for a relatively long time, as to allow the water vapor therein to begin to condense. Should this occur, the condensed water vapor would be delivered as water droplets to the blading channels of the turbocompressor and would cause damage through erosion and depositing of impurities contained in the gas flow. Axial blading is particularly endangered because higher speeds of the working medium to be compressed are generated relative to the blade surfaces driving the medium than is the case with the blading of a radial compressor.
Accordingly, it is an object of the invention to prevent the introduction of drops of condensate in a gaseous working medium into the blading of a compressor.
It is another object of the invention to provide a simple construction for removing drops of condensate from a flow of compressed gas leading to a turbocompressor from an intermediate cooler.
Briefly, the invention provides a multistage turbocompressor comprised of a compressor housing and an intermediate cooler outside the housing with a casing duct between the housing and cooler and a central duct enclosed within the casing duct and between the cooler and housing. The casing duct is connected to pass a flow of heated compressed gas from the housing, for example, from an initial compressor therein, to the cooler for cooling to suitable temperature for subsequent use. The central duct is connected to pass the flow of cooled compressed gas back to the housing, for example, to a second compressor. During passage through the casing duct, the heated gas heats the wall of the central duct. The resultant heat in the wall of the central duct then heats any condensate in the countercurrent flow of cooled gas within the central duct to vaporize the condensate. As a result, the return flow of gas becomes free of condensate.
Gas turbine equipment such as described in Swiss Pat. Nos. 2 l4,837 and 22 l ,377 have been known to use piping systems with a central duct disposed within a casing duct. However, these piping systems have been used to conduct a high-temperature gas through the central duct. In order to lower the temperature of a tube wall stressed by the pressure of the gas, a cooler gas has been conducted in the outer casing duct. ln this way, it has been possible to obtain thermal relief of the wall loaded by the high internal pressure, avoiding strength problems and leak-proofing difficulties. In accordance with the invention, the hot gas is conducted in the outer casing duct and the cool gas in the central duct. Thus, the tube wall dividing the casing duct from the central duct can be maintained at a hightemperature by means of the flow of not-yet-cooled gas. As a result, the flow of cool gas laden with drops of condensate is surrounded on all sides by a hightemperature wall. Upon encountering this wall, because of the increase of surface area, the drops become 2 vaporized before reaching the blading of the compres' sor.
The compressor may have an axial stage upstream of the exit point to the cooler of the medium being compressed, and may have a radial stage following the reentry of the cooler medium. The invention is of special importance for compressors with use axial stages following the re-entry of the cooled medium.
The function of the casing duct can be substantially facilitated by forming a bend in the casing duct as well as in the central duct since the drops of condensate will impact against the wall, and produce a greater surface area of contact. Thus revaporization can be accelerated.
The casing duct and central duct can advantageously be connected to the lower half of the housing where the housing is split in two halves. Also, it is possible to have two casing ducts disposed symmetrically of the perpendicular axial plane of the turborotor with each connected to the housing. Finally, a means may be disposed between the casing duct and the central duct to selectively introduce a variable amount of heated gas from the casing duct into the flow of cooled gas in the central duct in order to further promote the vaporization of the condensate drops.
These and other objects and advantages of the invention will become more apparent from the following detailed description taken in conjunction with the accompanying drawing in which:
FIG. 1 illustrates an axial cross-sectional view of a turbocompressor according to the invention;
FIG. 2 illustrates a cross-sectional view taken on the plane llll of FIG. 1.
FIG. 3 illustrates an axial cross-sectional view of a further turbocompressor construction according to the invention made as a purely axial compressor; and
FIG. 4 illustrates a cross-sectional view through a compressor with separate intermediate coolers disposed at both sides according to the invention.
Referring to H68. 1 and 2, an axial-radial turbocompressor includes in a housing 1 in which a rotor 2 is mounted and which has an inlet A for receiving air or a gas. The rotor 2 carries axial rotor rings 3 to 10 to compress air or a gas to a pressure at which the temperature rises to such an extent that intermediate cooling is necessary. The rotor 2 also carries radial stages ll and 12 of a radial compressor to compress the gas further to a final pressure after cooling. The housing I also has an outlet B at the end of the radial compressor for the exhaust of the compressed gas.
In order to intermediately cool the gas, a casing duct 13 is connected to the housing 1 between the axial stages 3 to 10 and the radial stages 11, 12 (FIG. 1) and extends to a cooler 14 (FIG. 2) to conduct the flow of heated compressed gas to the cooler 14. ln addition, a central duct 15 is enclosed within the casing duct 13 and extends from the cooler 14 to the housing 1 to conduct the flow of cooled compressed gas back to the housing and to the radial stages ll, 12. As shown, both ducts l3, 15 have a curved or bent position to deflect the respective flows of gas for purposes as described below.
Depending on the kind of gas to be compressed, the condition of the gas before reaching the compressor, and the condition desired at emergence from the compressor, the gas may be cooled in the intermediate cooler 14 to such an extent that the water contained in the gas before compression (or some other condens able inclusion) becomes condensed into drops. These drops are carried along by the gas flowing back into the compressor, and would, without an introduction of heat, only revaporize during the compression in the radial stage 11, and deposit non-vaporized impurities on the blade surfaces. Non-vaporized residues might even arrive in stage 12. As a result, and because of the high speeds at which the drops strike the rotor parts or other compressor parts, erosion and premature wear of these parts may occur.
By running the central duct 15 inside the casing duct 13, the wall of the central duct 15 is supplied with heat from the gas heated through compression in stages 3 to and flowing into the casing duct 13. As a result, the drops of liquid carried along by the cooled gas receive so much heat that they revaporize and, as vapor, can no longer cause damage to the radial rotors 11 and 12. The solid constituents are now dry, and are forced through the compressor without becoming deposited on the blades.
The vaporization of the drops of liquid in the central duct 15 can occur, in part, in the suspended state through the radiation of heat from the wall and also, in part, through contact with the duct wall. Because of the turbulence of the gas and the curved portions of the duct 15 some of the drops strike the heated duct wall and thereby become broken up. This gives the drops an enlarged surface area, thereby promoting more rapid vaporization. If there is a danger of a particularly great formation of liquid drops, then it is possible to install guide elements in the central duct to separate the drops out of the gas flow and conduct the drops against the wall. Such guide elements could also aid in the vaporization of the drops of condensate if heated to a suff' cient temperature by radiation from the duct walls.
Referring to FIG. 3, wherein like reference characters indicate like parts as above, an axial compressor having axial stages 16 to 21 follow the intermediate cooler (not shown). Axial stages are more endangered by drops in the gaseous working medium being com pressed and by deposits than are radial stages, and in their flow, undergo greater deviations than radial compressors. Naturally, the most endangered parts are the blades of the introduction-stator 22 first reached by the intermediately cooled gas. These blades do not receive the flow of gas from the central duct 15 as uniformly as do the blades of the following rotors 16 to 21 and stators 23 to 28.
Finally, referring to FIG. 4 wherein like reference characters indicate like parts as above, aa turbocompressor can be provided at each side of the housing 1 with an intermediate cooler 14. The housing 1 is split into two halves. with the connection of each cooler 14 made in the lower housing half 29 by flanges 30. This facilitates access to the rotor 2 for maintenance and overhauling work.
A means 31-33 is also provided between the casing duct 13 and the central duct 15 in order to selectively introduce a small variable amount of not-yetcooled medium being compressed from the casing duct 13 into the central duct 15. This means includes a pipe 31 connecting the casing duct 13 to the central duct 15, a series of outlets 32 in the pipe 31 to introduce the heated gas into the central duct 15 and a valve 33 for controlling the amount of flow through the pipe 31. This conducts so much heat to the cool gas in the central duct 15, which still contains drops, that any drops not reaching the wall and not sufficiently heat-irradiated by the wall become vaporized. An undesirable reheating of the cooled gas is not to be expected because the brought-in heat is used chiefly to vaporize the drops.
1 claim:
1. in a multistage turbocompressor having a compressor housing including an inlet and an outlet and an intermediate cooler outside said housing;
a casing duct connected between said housing and said cooler downstream of said inlet for passing a flow of heated compressed gas from said housing to said cooler for cooling therein, and
a central duct enclosed within said casing duct and connected between said cooler and said housing upstream of said outlet for passing the flow of cooled compressed gas from said cooler to said housing for passage out of said outlet.
2. In a multistage turbocompressor as set forth in claim 1, said casing duct and said central duct each having a bend therein.
3. In a multistage turbocompressor as set forth in claim 1, said housing being split in two halves in an axial plane and said ducts being connected to the lower half of said housing.
4. In a multistage turbocompressor as set forth in claim 3, wherein two said casing ducts are connected to said lower housing half symmetrically of a vertical axial plane of said housing.
5. In a multistage turbocompressor as set forth in claim 1, means connected between said casing duct and said central duct for selectively introducing a variable amount of heated gas from said casing duct into the flow of cooled gas in said central duct.
6. A multistage turbocompressor comprising a housing including an inlet and an outlet;
a first compressor in said housing downstream of said inlet for heating and compressing a flow of gas to a first pressure;
a second compressor in said housing downstream of said first compressor and upstream of said outlet for compressing the flow of gas to a higher pressure than said first pressure;
a cooler outside said housing for cooling the flow of heated gas;
a casing duct connected between said housing and said cooler for passing the flow of heated gas to said cooler from said first compressor; and
a central duct enclosed within said casing duct and connected between said cooler and said housing for passing the flow of cooled gas from said cooler to said second compressor.
7. A multistage turbocompressor as set forth in claim 6 wherein each duct has a bend therein for deflecting a respective flow of gas therein.
8. A multistage turbocompressor as set forth in claim 6 wherein said each compressor is an axial flow compressor.
9. A multistage turbocompressor as set forth in claim 6 wherein said first compressor is an axial flow compressor and said second compressor is a radial flow compressor.
10. A multistage turbocompressor as set forth in claim 6 further comprising a means connected between said casing duct and said central duct for selectively introducing a variable amount of heated gas from said 6 casing duct into the flow of cooled gas in said central to said cooler, duct. a central duct concentric to said casing duct and conll. A multistage turbocompressor comprising nected between said cooler and said housing for a compressor housing having an inlet and an outlet, passing the flow of cooled gas from said cooler to a first plurality of compressor stages in said housing 5 said housing downstream of said compressor adjacent and downstream of said inlet to receive stages. and and compress a flow of gas to a first pressure, a second plurality of compressor stages in said housa cooler outside said housing for cooling the flow of ing downstream of said first compressor stages and compressed gas, upstream of said outlet for compressing the flow of a casing duct connected between said housing and 10 gas from said cooler and central duct.
said cooler for passing the flow of compressed gas
Claims (11)
1. In a multistage turbocompressor having a compressor housing including an inlet and an outlet and an intermediate cooler outside said housing; a casing duct connected between said housing and said cooler downstream of said inlet for passing a flow of heated compressed gas from said housing to said cooler for cooling therein, and a central duct enclosed within said casing duct and connected between said cooler and said housing upstream of said outlet for passing the flow of cooled compressed gas from said cooler to said housing for passage out of said outlet.
2. In a multistage turbocompressor as set forth in claim 1, said casing duct and said central duct each having a bend therein.
3. In a multistage turbocompressor as set forth in claim 1, said housing being split in two halves in an axial plane and said ducts being connected to the lower half of said housing.
4. In a multistage turbocompressor as set forth in claim 3, wherein two said casing ducts are connected to said lower housing half symmetrically of a vertical axial plane of said housing.
5. In a multistage turbocompressor as set forth in claim 1, means connected between said casing duct and said central duct for selectively introducing a variable amount of heated gas from said casing duct into the flow of cooled gas in said central duct.
6. A multistage turbocompressor comprising a housing including an inlet and an outlet; a first compressor in said housing downstream of said inlet for heating and compressing a flow of gas to a first pressure; a second compressor in said housing downstream of said first compressor and upstream of said outlet for compressing the flow of gas to a higher pressure than said first pressure; a cooler outside said housing for cooling the flow of heated gas; a casing duct connected between said housing and said cooler for passing the flow of heated gas to said cooler from said first compressor; and a central duct enclosed within said casing duct and connected between said cooler and said housing for passing the flow of cooled gas from said cooler to said second compressor.
7. A multistage turbocompressor as set forth in claim 6 wherein each duct has a bend therein for deflecting a respective flow of gas therein.
8. A multistage turbocompressor as set forth in claim 6 wherein said each compressor is an axial flow compressor.
9. A multistage turbocompressor as set forth in claim 6 wherein said first compressor is an axial flow compressor and said second compressor is a radial flow compressor.
10. A multistage turbocompressor as set forth in claim 6 further comprising a means connected between said casing duct and said central duct for selectively introducing a variable amount of heated gas from said casing duct into the flow of cooled gas in said central duct.
11. A multistage turbocompressor comprising a compressor housing having an inlet and an outlet, a first plurality of compressor stages in said housing adjacent and downstream of said inlet to receive and compress a flow of gas to a first pressure, a cooler outside said housing for cooling the flow of compressed gas, a casing duct connected between said housing and said cooler for passing the flow of compressed gas to said cooler, a central duct concentric to said casing duct and connected between said cooler and said housing for passing the flow of cooled gas from said cooler to said housing downstream of said compressor stages, and a second plurality of compressor stages in said housing downstream of said first compressor stages and upstream of said outlet for compressing the flow of gas from said cooler and central duct.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CH1051772A CH553923A (en) | 1972-07-13 | 1972-07-13 | MULTI-STAGE TURBO COMPRESSOR WITH INTERCOOLING OF THE MEDIUM TO BE COMPRESSED. |
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US3892499A true US3892499A (en) | 1975-07-01 |
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US378428A Expired - Lifetime US3892499A (en) | 1972-07-13 | 1973-07-12 | Multistage turbocompressor having an intermediate cooler |
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US (1) | US3892499A (en) |
JP (1) | JPS5217881B2 (en) |
CH (1) | CH553923A (en) |
DE (1) | DE2235125B2 (en) |
FR (1) | FR2193427A5 (en) |
GB (1) | GB1383453A (en) |
IT (1) | IT991158B (en) |
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US4804885A (en) * | 1982-02-04 | 1989-02-14 | Tektronix, Inc. | X-ray attenuating ceramic materials |
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US3795458A (en) * | 1971-01-20 | 1974-03-05 | Bbc Sulzer Turbomaschinen | Multistage compressor |
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- 1972-07-13 CH CH1051772A patent/CH553923A/en not_active IP Right Cessation
- 1972-07-18 DE DE2235125A patent/DE2235125B2/en active Granted
- 1972-08-08 NL NL7210851A patent/NL7210851A/xx not_active Application Discontinuation
-
1973
- 1973-07-05 GB GB3214973A patent/GB1383453A/en not_active Expired
- 1973-07-10 FR FR7325218A patent/FR2193427A5/fr not_active Expired
- 1973-07-12 JP JP48078857A patent/JPS5217881B2/ja not_active Expired
- 1973-07-12 IT IT26506/73A patent/IT991158B/en active
- 1973-07-12 US US378428A patent/US3892499A/en not_active Expired - Lifetime
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US2563745A (en) * | 1942-03-06 | 1951-08-07 | Lockheed Aircraft Corp | Variable area nozzle for power plants |
US2396484A (en) * | 1944-07-24 | 1946-03-12 | Allis Chalmers Mfg Co | Intercooled compressing apparatus |
US2619279A (en) * | 1948-07-16 | 1952-11-25 | Sulzer Ag | Axial flow compressor |
US2925954A (en) * | 1956-03-29 | 1960-02-23 | Escher Wyss Ag | Compressor group with intercooler |
US3795458A (en) * | 1971-01-20 | 1974-03-05 | Bbc Sulzer Turbomaschinen | Multistage compressor |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4592204A (en) * | 1978-10-26 | 1986-06-03 | Rice Ivan G | Compression intercooled high cycle pressure ratio gas generator for combined cycles |
DE3424925C1 (en) * | 1984-05-16 | 1985-10-17 | Sulzer-Escher Wyss GmbH, 7980 Ravensburg | Turbo engine with at least one radial flow rotor |
US4936109A (en) * | 1986-10-06 | 1990-06-26 | Columbia Energy Storage, Inc. | System and method for reducing gas compressor energy requirements |
WO2000039441A1 (en) * | 1998-12-24 | 2000-07-06 | Alliedsignal Inc. | Apparatus and method to increase turbine power |
US6363706B1 (en) | 1998-12-24 | 2002-04-02 | Alliedsignal | Apparatus and method to increase turbine power |
US8192144B2 (en) * | 2007-09-28 | 2012-06-05 | Hitachi, Ltd. | Compressor and heat pump system |
US20090087298A1 (en) * | 2007-09-28 | 2009-04-02 | Takanori Shibata | Compressor and heat pump system |
US8764385B2 (en) * | 2008-07-01 | 2014-07-01 | Snecma | Axial-centrifugal compressor having system for controlling play |
US20110129332A1 (en) * | 2008-07-01 | 2011-06-02 | Snecma | Axial-centrifugal compressor having system for controlling play |
US20100189551A1 (en) * | 2009-01-29 | 2010-07-29 | General Electric Company | Systems and Methods of Reducing Heat Loss from a Gas Turbine During Shutdown |
US8210801B2 (en) * | 2009-01-29 | 2012-07-03 | General Electric Company | Systems and methods of reducing heat loss from a gas turbine during shutdown |
US9039349B2 (en) * | 2009-04-28 | 2015-05-26 | Concepts Eti, Inc. | Turbocompressor and system for a supercritical-fluid cycle |
US20120034067A1 (en) * | 2009-04-28 | 2012-02-09 | Concepts Eti, Inc. | Turbocompressor and System for a Supercritical-Fluid Cycle |
US8075245B2 (en) | 2009-05-27 | 2011-12-13 | Dresser-Rand Company | Removal of moisture from process gas |
WO2010138403A1 (en) * | 2009-05-27 | 2010-12-02 | Dresser-Rand Company | Removal of moisture from process gas |
US20100303605A1 (en) * | 2009-05-27 | 2010-12-02 | Dresser-Rand Company | Removal of moisture from process gas |
AU2010254296B2 (en) * | 2009-05-27 | 2015-12-17 | Dresser-Rand Company | Removal of moisture from process gas |
CN109751282A (en) * | 2019-02-02 | 2019-05-14 | 沈阳透平机械股份有限公司 | A kind of axial-flow-centrifugal formula air compressor of axial admission |
US20220228593A1 (en) * | 2019-08-07 | 2022-07-21 | Carrier Corporation | Axial and downstream compressor assembly |
US11965514B2 (en) * | 2019-08-07 | 2024-04-23 | Carrier Corporation | Axial and downstream compressor assembly |
Also Published As
Publication number | Publication date |
---|---|
GB1383453A (en) | 1974-02-12 |
CH553923A (en) | 1974-09-13 |
DE2235125B2 (en) | 1974-07-04 |
DE2235125A1 (en) | 1974-02-07 |
DE2235125C3 (en) | 1978-10-05 |
JPS5217881B2 (en) | 1977-05-18 |
IT991158B (en) | 1975-07-30 |
JPS4958406A (en) | 1974-06-06 |
FR2193427A5 (en) | 1974-02-15 |
NL7210851A (en) | 1974-01-15 |
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Owner name: SULZER-ESCHER WYSS AG, A CORP OF SWITZERLAND, SWIT Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:BROWN BOVERI-SULZER TURBOMACHINERY LIMITED, JAKOB WYDLER, LIQUIDATOR;REEL/FRAME:005221/0890 Effective date: 19890530 |