GB2036178A - Regenerative rotodynamic pumps and compressors - Google Patents

Regenerative rotodynamic pumps and compressors Download PDF

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Publication number
GB2036178A
GB2036178A GB7940287A GB7940287A GB2036178A GB 2036178 A GB2036178 A GB 2036178A GB 7940287 A GB7940287 A GB 7940287A GB 7940287 A GB7940287 A GB 7940287A GB 2036178 A GB2036178 A GB 2036178A
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United Kingdom
Prior art keywords
impeller
machine according
annular
blades
casing
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Granted
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GB7940287A
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GB2036178B (en
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Compair Industrial Ltd
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Compair Industrial Ltd
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Priority to GB7940287A priority Critical patent/GB2036178B/en
Publication of GB2036178A publication Critical patent/GB2036178A/en
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Publication of GB2036178B publication Critical patent/GB2036178B/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D5/00Pumps with circumferential or transverse flow
    • F04D5/002Regenerative pumps
    • F04D5/003Regenerative pumps of multistage type
    • F04D5/006Regenerative pumps of multistage type the stages being axially offset
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D23/00Other rotary non-positive-displacement pumps
    • F04D23/008Regenerative pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/18Rotors
    • F04D29/188Rotors specially for regenerative pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D5/00Pumps with circumferential or transverse flow
    • F04D5/002Regenerative pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D5/00Pumps with circumferential or transverse flow
    • F04D5/002Regenerative pumps
    • F04D5/003Regenerative pumps of multistage type
    • F04D5/005Regenerative pumps of multistage type the stages being radially offset

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Abstract

An annular cavity or scooped- out recess 12A formed in the side wall of the impeller 11 and facing an annular side channel 13A contains impeller blades 18A which are curved in radial cross-section so as to impart a forward peripheral component of velocity to the fluid at the trailing edges of the blades which is greater than the forward velocity of the trailing edges. As shown, the impeller may be double-sided, with a further recess 12B and blades 18B co-operating with a further side channel 13B. <IMAGE>

Description

SPECIFICATION Improvements in or relating to regenerative rotodynamic machines This invention relates to regenerative rotodynamic machines, and more specially to regenerative pumps and compressors.
A regenerative or peripheral pump is a rotodynamic machine which permits a head equivalent to that of several centrifugal stages to be obtained from a single rotor with comparable tip seeds. The impeller can take the form of a disc with a set of vanes projecting axially at each side near the disc periphery.
Around the greater portion of the periphery the vanes project into an annular channel of which the cross sectional area is greater than that of the impeller vanes. At one sector between the inlet and discharge the annular channel is reduced to a close running clearance around the impeller. This sector is called the stripper seal and its function is to separate the inlet and discharge ports, thereby forcing the fluid out through the discharge port. The stripper allows only the fluid between the impeller vanes to pass through to the inlet.
The advantage of pumps of this type lies in the generation of a high head at low flow rates. They have a very low specific speed.
Although their efficiency is not very high, being usually less than 50%, pumps of this type have found many applications in industry where it is preferred to use rotodynamic pumps in place of positive displacement pumps for duties requiring a high head at low flow rates. Their simplicity, and the absence of problems due to lubrication and wear, give advantages over positive displacement pumps, despite the lower efficiency.
The regenerative pump has been adapted for the compression of gas. The advantage lies in the low specific speed giving a high pressure ratio together with a low flow rate for a given size of machine. Further advantages are oil free operation and freedom from stall or surge instability.
In such a compressor, the gas follows a helical path through the annular channel and passes through the vanes a number of times in its peripheral path from the inlet port to the discharge port. Each passage through the vanes may be regarded as a stage of compression and thus the equivalent of several stages of compression can be obtained from a single impeller. This pumping process, however, cannot be considered as efficient. The fluid between the vanes is thrown out and across the annular channel and violent mixing occurs, the angular momentum acquired by the fluid in its passage between the vanes being transferred to the fluid in the annular channel.
The mixing process is accompanied by the production of a great deal of turbulence and this implies an undesirable waste of power.
Several theories of the fluid-dynamic mech anism of a regenerative pump have been published. These theories have been reviewed and compared by Senoo (A.S.M.E. Trans. Vol.
78, 1956, pp. 1091-1102). Differences oc cur in the assumptions made, but in principle the various theories appear to be compatible.
Senoo and Inversen (A.S.M.E. Trans. Vol. 77, 1955, pp 19-28) consider turbulent friction between the moving impeller and the fluid as the primary force causing the pumping action.
Wilson, Santalo and Oelrich (A.S.M.E. Trans.
Vol. 77, 1955, pp 1303-1316) regard the mechanism as based on a circulatory flow between the impeller and the fluid in the casing with an exchange of momentum be tween the fluid passing through the impeller and the fluid in the casing.
More recently, compressors with consider ably better efficiency have been proposed in which the conventional radial vanes are re placed by aerodynamic blading. The annular channel is provided with a core to assist in guiding the fluid so that it circulates through the blading with a minimum of loss. The core also acts as a shroud closely surrounding the blades at their tips to reduce losses due to the formation of vortices at the tips of the blades.
Such an arrangement is described, for in stance, in British Patent Specification No.
1237363.
It is an object of this invention to achieve further important improvements in regenera tive rotodynamic machines, and especially to make possible a range of compressors with aerodynamic blading that possess commercial advantages.
According to the present invention, in a regenerative rotodynamic machine, a rotary disc-like impeller has a portion adjacent its periphery that extends radially through an annular chamber in the casing concentric with the impeller which chamber is wider than the impeller so that an annular side channel is thereby provided in the casing on at least one side of the impeller, and radially inward of its outer peripheral surface the portion of the impeller within the annular chamber is formed, on the side where lies said annular side channel, with an annular cavity or scooped out recess in its side wall in which is disposed a ring of aerodynamic blades that have a radial extent less than the radial extent of the cavity or recess, the fluid flow passing peripherally around the annular chamber from an inlet to an outlet and also during this passage circulating a number of times radially outward through the aerodynamic blading in the impeller cavity and radially inward in the annular side channel alongside the impeller outside the cavity, the forward peripheral component of velocity of the fluid at the trailing edges of the blades being greater than the forward velocity of said trailing edges.
In the preferred embodiment, the annular chamber is divided by the impeller into two annular side channels, one on each side of the impeller, and the impeller has annular cavities, with rings of blading disposed therein, on both sides of its peripheral region. The blades being situated in scooped out recesses in the impeller gives the particular advantage that the gas flow emerging from the blading is still within these scooped out recesses and does not come into frictional contact with the stationary outer peripheral wall of the annular chamber. Therefore, friction is reduced as compared with prior machines in which the gas leaving the blading impinges directly on the stationary wall of the annular chamber. A further advantage accrues if the impeller disc complete with blading is manufactured as a single integral machine part by, for example, die-casting.A core or blade tip shroud can then be provided in the annular channel at each side of the impeller by securing a shroud ring to the tips of the blades. An alternative method of manufacture, also having advantages, is to die-cast the impeller disc without blading, and to cast the blading integrally with the shroud rings, each set of blading, complete with the respective shroud ring, being afterwards secured into the respective impeller recess or cavity.
Arrangements of compressor in accordance with the invention will now be described, by way of example, with reference to the accompanying drawings, in which: Figure 1 is a diagrammatic cross-section of a regenerative compressor according to the invention, Figures 2 and 3 show, respectively, the interior and exterior of the top half of the casing of an actual compressor embodying the principles of Fig. 1, Figures 4 and 5 are corresponding views of the bottom half of the compresor casing, Figure 6 is a plan view of the compressor impeller, Figures 7 and 8 are sectional views on the lines 7-7 and 8-8, respectively, of Fig. 6, Figure 9 is a diagram of the aerodynamic blade profile, Figure 10 is a diagrammatic representation of the blade velocities and flow angles, Figure ii 1 shows a second embodiment in which the compressor has two impellers to operate as successive stages, and Figure 12 shows, as a third embodiment, an alternative form of multistage compressor.
In the drawings, Fig. 1 is a diagrammatic view illustrating the operation of a regenerative compressor of which the actual casing members and impeller are shown in Figs. 2 to 8.
Referring firstly to Fig. 1, this shows diagrammatically a simple single impeller regenerative compressor according to the invention.
The impeller 1 housed in a split casing 25 is driven by a shaft 10 and consists of a disc with aerodynamic blades 18A, 1 8B provided within scooped out regions 12A, 1 2B at each side of the disc just radially inward of the discs periphery. The bladed margin of the impeller projects into an annular chamber 1 3 in the compressor casing 25 which is wider than the impeller and has at its outer periphery an inward4acing cylindrical surface 14 which is closely approached by the cylindrical peripheral surface 1 5 of the impeller 11, thereby dividing the chamber 1 3 into two separated side channels 13A, 13B, each of roughly oval cross-section, that are located on opposite sides of the impeller disc 1 and are each defined partly by the wall of the chamber 1 3 and partly by the contour of the respective scooped out side portion 1 2A or 1 2B of the impeller 11 that contains the blades 1 8A or 18B. The blades extend approximately half-way across the respective side channel 13A, 1 3B and are designed to turn the fluid through an angle of well in excess of 90 as its flows radially outward through the blading, setting up a circulation in each side channel 13A, 1 3B as indicated by the arrows F.Each annular side channel has a central core 16A, 1 6B to assist in guiding the fluid so that it circulates through the blading with a minimum of loss. Each core 16A, 1 6B is in the form of a shroud ring placed against the blade tips to eliminate loss due to formation of vortices at the tips of the blades. The shroud rings 16A, 1 6B are secured to the impeller blades 18A, 1 8B by screws locating in bosses 1 7 on the impeller (Fig. 8). Alternatively, the shroud rings may be stationary and supported on a number of small pillars bolted to the sides of the casing.
The fluid enters the annular chamber 1 3 through a port 1 9 in the wall of the casing 25 which leads to an inlet chamber 20 communicating with both of the channels 13A, 1 3B at their outer peripheries. The fluid leaves the annular channels 13A, 1 3B through an outlet 21 (Figs. 2 to 5) which is followed by a conical diffuser 26 to obtain pressure recovery. Between the inlet and outlet, the stripper seal 22 (Figs. 2 and 4) is formed by shaping the interior of the casing walls so that they aproach closely to the sides of the impeller all the way out to its periphery 1 5. Alternatively, the stripper seal can be formed by the addition of a completely separate stripper element.
Since high pressure gas is then trapped in the scooped cavities 1 2A, 1 2B of the impeller, relieving passages 28 are provided in the casing walls that communicate with the chamber 1 3 at various locations.
Radially inward of the scooped cavities 12A, 12B and blading 18A, 18B, the impeller 11 is formed as an annular dish, with a hollow interior 23 closed by an annular plate 27, as seen in Figs. 1 and 7. Since gas may creep down one side of the impeller more than the other and create a pressure differen tial across the rotor disc, pressure equalising holes 24 are provided.
Between the inlet and outlet ports 19, 21 the fluid being compressed passes a number of times through the blading 18A, 18B. During each passage a quantity of energy is transferred from the impeller to the fluid. The rate of flow through the blading is self-adjusting in the sense that the velocity through the blade channels tends to increase until the rate of energy transfer reaches the value needed to generate the pressure difference between the inlet and outlet ports. An increase in the pressure difference causes corresponding increases in both the number of passages through the blading and the energy transferred at each passage. The rate of energy transfer tends to vary as the square of the velocity relative to the blades.By equating the power transferred from the blading to the fluid with the power needed to generate the pressure difference across the inlet and outlet ports, the flow velocities in the annular channels 1 3A, 1 3B can be estimated. This information serves as a useful guide towards the optimum design of the blading.
Referring to Fig.10, it is seen that the fluid enters and leaves the blading with relative velocities W, and W2 and with inlet and outlet fluid angles of ss, and p2 If Vui and Vu2 are, respectively, the peripheral components of the absolute velocities of the fluid at the leading and trailing edges of the blading, and U, and U2 are the peripheral velocities of the leading and trailing edges, then: Vu1 = U, - W, sin ss, Vu2 = U2 + W2 sin ss2 The peripheral or forward component of velocity of the gas on leaving the blades is greater than the blade velocity.As soon as the gas emerges from the blades, it comes under the influence of the peripheral pressure gradient and during its transverse passage around the annular channel its peripheral velocity is progressively reduced until it re-enters the blading to receive another impulse. As seen in Fig. 9, for ease of manufacture the surfaces of the aerodynamic blades 1 2A, 1 2B are formed of successions of circular arcs. In the example illustrated, the inner surface 30 of the blade is formed as a single arc while the outer surface 31 is formed as a central 80 arc flanked by two 15 arcs and then two 18 arcs.
In the illustrated embodiments, the aerodynamic blades 1 8A, 1 8B are die-cast integrally with the impeller disc 11. However, as already indicated, a possible alternative is to die-cast the impeller disc with empty cavities 1 2A, 1 2B and to form the blading separately, each set of blading being cast integrally with its respective shroud ring 16A or 16B and afterwards secured, e.g. by screws, into the appropriate cavity 1 2A or 12B.
Two or more impellers can be mounted on a common drive shaft to provide a multi-stage or multi-banked compressor. Fig. 11 shows a compressor with two impellers 32, 33 of different sizes on a common drive shaft 34.
However, a more interesting possibility is the arrangement shown in Fig. 12, in which a single impeller 35 carries, radially inward of its periphery, two sets of blading 36, 37 disposed in side cavities 38, 39 (similarly to the blading 18A, 18B of the embodiment of Figs. 2 to 8) and, in addition, further blading 40 formed at its periphery. In this case, a gap 41 exists between the impeller periphery and the inner circumferential wall 42 of the casing 43, uniting the two annular side channels 44, 45 at opposite sides of the impeller rim.
Such a machine can be staged in any desired manner. That is to say, the fluid being compressed can be passed in succession through the three sets of blading 36, 37, 40 in any order. In the example illustrated, the circled numbers 1, 2 and 3 indicate that the order proposed is that the fluid shall be compressed first by the peripheral blading 40, then by one set of side blading 36 and thirdly by the other set of side blading 37.
Whereas the machines shown in the drawings have double-sided impellers, it will be understood that it is possible to have blading only on one side. By employing a split impeller built up from two halves a range of capacities readily becomes available using only two kinds of impeller casting. Thus, half the capacity of a double-sided impeller is obtained by fixing together a bladed half-impeller and a blank half, twice the capacity is obtained from two double-sided impellers in bank, and 1+ times the capacity is given by two impellers one of which has a blank side.
Machines according to the invention are balanced and vibration free and, being comparatively inexpensive to build, provide a quieter alternative to the Roots blower. Existing regenerative compressors are equally smooth running but not so efficient. Thus, such prior machines give a maximum of 8 p.s.i. in one stage whereas machines according to the invention will give 10 p.s.i. and upwards, and also can be employed to pull a vacuum. A machine such as that shown in Figs. 2 to 8 is particularly easy to manufacture, the parts being formed by simple die-casting, and, as already explained, friction is reduced at the periphery of the impeller.

Claims (16)

1. A regenerative rotodynamic machine, wherein a rotary disc-like impeller has a portion adjacent its periphery that extends radially through an annular chamber in the casing concentric with the impeller which chamber is wider than the impeller so that an annular side channel is thereby provided in the casing on at least one side of the impeller, and radially inward of its outer peripheral surface the portion of the impeller within the annular chamber is formed, on the side where lies said annular side channel, with an annular cavity or scooped out recess in its side wall in which is disposed a ring of aerodynamic blades that have a radial extent less than the radial extent of the cavity or recess, the fluid flow passing peripherally around the annular chamber from an inlet to an outlet and also during this passage circulating a number of times radially outward through the aerodynamic blading in the impeller cavity and radially inward in the annular side channel alongside the impeller outside the cavity, the forward peripheral component of velocity of the fluid at the trailing edges of the blades being greater than the forward velocity of said trailing edges.
2. A machine according to claim 1, wherein a shroud ring is disposed adjacent to the blade tips of the ring of aerodynamic blades, the shroud ring constituting a core within the annular channel around which the fluid circulates.
3. A machine according to claim 2, wherein the shroud ring is secured to the blades and rotates with the impeller.
4. A machine according to claim 2, wherein the shroud ring is stationary, being mounted in the casing.
5. A machine according to any one of the preceding claims, wherein the aerodynamic blades are cast integrally with the impeller.
6. A machine according to claim 2, wherein the blades are cast integrally with the shroud ring, and separately from the impeller, the shroud ring and blades being secured to the impeller.
7. A machine according to any one of the preceding claims, wherein the annular chamber is divided by the impeller into two annular side channels, one on each side of the impeller, and the impeller bears two rings of aerodynamic blades disposed in respective cavities or recesses in opposite sides of the impeller.
8. A machine according to any one of the preceding claims, wherein the outer peripheral surface of the impeller is in close running clearance with the inward facing outer peripheral wall of the casing.
9. A machine according to any one of the preceding claims, wherein the aerodynamic blades have an angle between the entry and exit flows of each blade greater than 90 .
10. A machine according to any one of the preceding claims, wherein a sector of the annular chamber between the inlet and the outlet is occupied by a stripper seal, and relieving passages are provided in the casing between the stripper seal sector of the annular chamber and other locations around the annu lar chamber remote from the stripper seal.
11. A machine according to claim 10, having a split casing and wherein the stripper seal is cast integrally with the parts of the casing.
12. A machine according to claim 10, wherein the stripper seal is formed by an insert piece or pieces secured in the sector of the annular chamber between the inlet and outlet.
1 3. A machine according to any one of the preceding claims, wherein the impeller is provided with two rings of aerodynamic blades in respective annular scoop recesses in opposite sides of the impeller, and a third ring of blades at the impeller periphery operating in a further annular channel in the casing.
1 4. A machine according to any one of the preceding claims, wherein each curved surface of each aerodynamic blade is formed from one or more circular arcs.
1 5. A machine according to any one of the preceding claims, comprising two or more impellers, of the same or different sizes, on a common shaft, each impeller bearing at least one ring of aerodynamic blades disposed in a scoop recess in the side of the impeller and operating in a respective annular channel in the casing.
16. A regenerative compressor, substantially as described with reference to Fig. 1 or Figs. 2 to 9, or Fig. 11, or Fig. 12, of the accompanying drawings.
GB7940287A 1978-11-28 1979-11-21 Regenerative rotodynamic pumps and compressors Expired GB2036178B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB7940287A GB2036178B (en) 1978-11-28 1979-11-21 Regenerative rotodynamic pumps and compressors

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB7846419 1978-11-28
GB7940287A GB2036178B (en) 1978-11-28 1979-11-21 Regenerative rotodynamic pumps and compressors

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GB2036178A true GB2036178A (en) 1980-06-25
GB2036178B GB2036178B (en) 1983-03-23

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4441855A (en) * 1980-03-20 1984-04-10 The Secretary Of State For Defence In Her Britannic Majesty's Government Of The United Kingdom Of Great Britain And Northern Ireland Compressors
GB2134598A (en) * 1983-02-02 1984-08-15 Bosch Gmbh Robert Fuel pumps for internal- combustion engines
US5310308A (en) * 1993-10-04 1994-05-10 Ford Motor Company Automotive fuel pump housing with rotary pumping element
FR2721978A1 (en) * 1994-06-03 1996-01-05 Coltec Ind Inc REGENERATION PUMP WITH EXTENDED OPERATING RANGE
US6422808B1 (en) 1994-06-03 2002-07-23 Borgwarner Inc. Regenerative pump having vanes and side channels particularly shaped to direct fluid flow
EP1286041A2 (en) * 2001-07-31 2003-02-26 Denso Corporation Impeller and turbine type fuel pump
WO2020104226A1 (en) * 2018-11-22 2020-05-28 Robert Bosch Gmbh Side-channel compressor for a fuel cell system for conveying and/or compressing a gaseous medium

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9249806B2 (en) 2011-02-04 2016-02-02 Ti Group Automotive Systems, L.L.C. Impeller and fluid pump

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4441855A (en) * 1980-03-20 1984-04-10 The Secretary Of State For Defence In Her Britannic Majesty's Government Of The United Kingdom Of Great Britain And Northern Ireland Compressors
GB2134598A (en) * 1983-02-02 1984-08-15 Bosch Gmbh Robert Fuel pumps for internal- combustion engines
US5310308A (en) * 1993-10-04 1994-05-10 Ford Motor Company Automotive fuel pump housing with rotary pumping element
FR2721978A1 (en) * 1994-06-03 1996-01-05 Coltec Ind Inc REGENERATION PUMP WITH EXTENDED OPERATING RANGE
FR2787147A1 (en) * 1994-06-03 2000-06-16 Borg Warner Automotive REGENERATION PUMP WITH EXTENDED RANGE OF OPERATION
US6422808B1 (en) 1994-06-03 2002-07-23 Borgwarner Inc. Regenerative pump having vanes and side channels particularly shaped to direct fluid flow
EP1286041A2 (en) * 2001-07-31 2003-02-26 Denso Corporation Impeller and turbine type fuel pump
EP1286041A3 (en) * 2001-07-31 2003-04-09 Denso Corporation Impeller and turbine type fuel pump
US6767179B2 (en) 2001-07-31 2004-07-27 Denso Corporation Impeller and turbine type fuel pump
WO2020104226A1 (en) * 2018-11-22 2020-05-28 Robert Bosch Gmbh Side-channel compressor for a fuel cell system for conveying and/or compressing a gaseous medium
CN113167285A (en) * 2018-11-22 2021-07-23 罗伯特·博世有限公司 Side channel compressor for conveying and/or compressing gaseous medium for fuel cell system

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