The present invention relates to multi-stage compressors. More specifically, the present invention is concerned with multi-stage compressors of variable pumping capacity and pressure ratios.
Compressors used in most industries are often required to vary both their pumping capacity and their pressure ratios. In the particular instance of the air conditioning and refrigeration industries, cooling or heating loads vary throughout the year for example, and the required pressure ratios vary accordingly as the condensing temperatures and evaporating temperatures vary. Typically, as the outside ambient temperature rises, so do the required pressure ratio and the required capacity. Moreover, the higher the pressure ratio, the less flexible the compressor becomes in its ability to unload, resulting in a smaller operating window and in more energy being required to pump the gas.
Traditionally, centrifugal compressors are designed to be efficient in achieving a specific “flow” and “head” at a predetermined “design point”. When conditions change, a compressor must then operate at “off design” in a very wide range of conditions, resulting generally in worse energy efficiency. The efficiency, capacity, lift and range of a compressor can be improved in off design conditions by introducing means to vary the flow. In some industrial processes, compressors may have to supply air or other types of gas at different volumes and different pressures, depending on a relevant demand at the time.
Although typically more efficient than other forms of compressors, centrifugal compressors are also less flexible in simultaneously handling high-pressure ratios and low capacity demand. Centrifugal compressors can supply high-pressure ratios by adding more stages of compression in series with one another. While this method of pumping can allow high-pressure ratios, it also limits the ability for the compressors to unload without going into a condition known as surge.
As known in the art, when designing a centrifugal compressor, it is much easier to design a single stage compressor than a two-stage compressor, and it is much easier to develop a two-stage compressor than a three-stage compressor, especially when all stages are mounted on a same rotating shaft and operate at a same rotational speed, and it is much easier to develop a three-stage compressor than a four-stage compressor, etc.
Another difficulty in designing a multi-stage compressor is to design it so that it may handle high pressure ratios while having a required turndown minimum capability.
There is therefore still a need in the art for a multi-stage compressor.
More specifically, there is provided a multi-stage compressor, comprising a rotating shaft, a primary pumping circuit comprising at least one primary stage, the at least one primary stage being coupled to the rotating shaft; and a secondary pumping circuit comprising at least one secondary stage, wherein each one of the at least one secondary stage is adapted to be coupled and un-coupled from the rotating shaft.
There is further provided a method for adjusting the capacity of a multi-stage compressor comprising a rotating shaft and a primary pumping circuit comprising at least one primary stage coupled to the rotating shaft, comprising determining current capacity requirements of the multi-stage compressor; coupling at least one secondary stage to the rotating shaft to increase the capacity, and decoupling at least one of the at least one secondary stage from the rotating shaft to decrease the capacity, as determined by the previous step.
There is further provided a coupling assembling for coupling a secondary stage to a rotating shaft of a compressor comprising a primary stage, comprising a permanent magnet inserted into either one of the end of the rotating shaft or the secondary impeller and a magnetic piece inserted into the remaining one of the secondary impeller or the end of the rotating shaft, the secondary stage being held onto the rotating shaft by magnetic forces between the permanent magnet and the magnetic piece.
There is further provided a coupling assembly for coupling a secondary impeller to a rotating shaft of a compressor comprising a primary stage, comprising a first magnet inserted in the rotating shaft; and a second magnet inserted in the secondary impeller, the secondary impeller attaching itself to the rotating shaft by the attraction strength between opposing poles of the first and second magnets.
There is further provided an assembly for coupling and decoupling a secondary impeller to a rotating shaft of a compressor comprising a primary stage, comprising a magnet inserted in the rotating shaft; and an electromagnet supported by the secondary impeller, wherein when the electromagnet is on, a force between the electromagnet and the magnet drives the secondary impeller away from the rotating shaft, and when the electromagnet is off the secondary impeller is attracted to the magnet embedded in the rotating shaft and the secondary impeller couples to the rotating shaft.
Other objects, advantages and features of the present invention will become more apparent upon reading of the following non-restrictive description of embodiments thereof, given by way of example only with reference to the accompanying drawings.
In the appended drawings:
The present invention is illustrated in further details by the following non-limiting examples.
There is generally provided a system and a method for adding and subtracting stages of compression to a compressor as, and when, the compressor requires them.
For example, if the compressor needs only a low pressure ratio, then the system and method allow the compressor to operate with only a primary pumping circuit spinning, while available additional stages, forming a secondary pumping circuit, and which may be required at other times when the required pressure ratios increase, being decoupled from the rotating shaft, so that the compressor only pumps at its most efficient and flexible point.
On the contrary, when a higher pressure ratio is required, such as when outside ambient temperatures increase in the middle of summer in an air-conditioning installation for example, since the additional stages are required in order to reach higher pressure ratios, the system and method allow to re-couple them to the rotating shaft, thereby allowing these additional stages to spin with the rotating shaft, thereby allowing the compressor to reach the required higher pressure ratios.
According to the present invention, each one of the primary pumping circuit and the secondary pumping circuit of the compressor may include one or more stages. If the secondary pumping circuit comprises more than one stage, then these stages may be decoupled or re-coupled to the rotating shaft, either successively or at the same time, as will be further discussed.
It may be desirable that the secondary stages be positioned with their suction inlet facing in the direction along the rotating shaft axis, since, as the impellers have a natural tendency to drive themselves towards the direction of the incoming gas, this may add to the frictional force of the coupling's two mating surfaces and reduce the likelihood of any possible slippage between the impeller and the rotating shaft. It is important that all impellers spin at the same RPM (revolutions per minute), as, if the secondary impeller happens to slip and turn at a slower speed, this may lead to compressor inefficiencies and wear between the mating surfaces of the rotating shaft and the secondary impeller.
Moreover, by incorporating variable frequency drives, inlet guide vanes, and/or variable diffusers, the compressor loading and unloading capability may further be increased. Indeed, in compressors, such as those described in U.S. Pat. No. 5,857,348 for example, the unloading mechanism and pressure ratio control is primarily handled by varying the speed of the compressor: in conditions where the compressor is likely to experience a surge condition, then inlet guide vanes, or exit wall diffusers, start to close off, thereby allowing the compressor to reduce its pumping capacity to a greater extent than it could have had these devices not been activated (see
A single or multiple bypass port may be provided into the discharge gas stream of the secondary pumping circuit, to allow the gas stream to bypass the non-rotating secondary impeller(s) and thus reduce unnecessary loads onto the non-rotating secondary impeller(s) and increase the overall compressor efficiency by thus eliminating associated frictional losses.
As an alternative to bypass ports, the outer sealing surface of the impeller, referred to as the shroud, may be moved away from the impeller by a distance where the frictional losses become insignificant, in which case no bypass is required. As known to people in the art, the distance between the impeller and the shroud is a most important clearance parameter in a centrifugal compressor and should be kept as tight as possible, since, the tighter the distance, the more efficient the compressor's performance.
In cases when the shroud 46 is brazed to the impeller or otherwise becomes part of the impeller, the gas seal may be provided by some other means, such as a labyrinth seal, as known in the art.
In the case of an open shrouded design as shown in
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The examples shown in
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The secondary impellers H and I may be decoupled or re-coupled simultaneously or not, depending on whether the required pressure ratios are the same at each end of the rotating shaft 14, and this of course depends on whether the discharge gas is being pumped into the same circuit or not. For example, in
An interstage port 70 may be provided between two consecutive stages, as shown in
The coupling and uncoupling to and from the rotating shaft 14 of the compressor may be done in several ways, by using mechanical, magnetic or electromechanical or electromagnetic means. For the purpose of this description, the secondary stages are held onto the rotating shaft 14 by means of magnetic forces in
In
Alternatively, a first magnet could be inserted in the rotating shaft 14 and a second magnet could be inserted in the secondary impeller 32, the secondary impeller 32 attaching itself to the rotating shaft 14 by means of the attraction strength between the opposing poles of the two magnets.
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It is possible to use one or two secondary shrouded impellers 32 on its secondary rotating shaft in such a way as to be able to incorporate significantly more impeller mass and axial overhang whilst reducing the rotational frictional losses by means of utilizing additional mechanical or passive or active magnetic bearings 55 or a combination thereof (see
It may also be possible to manufacture either the rotating shaft or the secondary impeller out of a magnetic material, such as a magnetic metal, and have the permanent magnet incorporated into the remaining part of one of the shaft or the secondary impeller.
Coupling sprocket or gear or clutch or rough surface or some other way such as additional magnets may be further provided to eliminate the risk of slippage between the rotating shaft 14 and the secondary impeller 32, which may occur under high load conditions. In
In order to simplify the design of the bypass port and the decoupling assembly, it may be desirable to mechanically or electrically link the two devices together or to incorporate them into a single device, as shown in
The compressor shown in
There are many ways that a decision may be made to determine if secondary stages should be decoupled or re-coupled to the rotating shaft of a compressor, as described hereinabove. Once this decision is made, the compressor shuts down, or at least slows down to a point where the additional stages can be decoupled or re-coupled to the rotating shaft without putting the impellers at risk of damaging themselves.
One such way of determining whether a secondary pumping circuit should be coupled or decoupled may comprise, for example, determining the ambient temperature. For example, the compressor may be made to shut down once the ambient temperature reaches a threshold temperature, such as 104° Fahrenheit (40° Celsius) for instance, for re-coupling secondary impeller(s) to the rotating shaft, before the compressor is restarted with the additional stage(s) assembled to the primary stage(s) previously operating alone. In contrast, when the ambient temperature drops to a threshold temperature such as 95° Fahrenheit (35° Celsius) for instance, the compressor may be made to shut or slow down for decoupling the secondary impeller(s) from the rotating shaft, before the compressor is restarted, the secondary impeller(s) being this time inactivated. The control and system logic not being specifically disclosed herein but being known to those in the particular field of application.
The present method of operating a compressor not only allows the compressor to achieve required high pressure ratios, but also allows additional stages of a secondary circuit to be left out when they are no longer required, which in turn allows the compressor to unload its pumping capacity much lower than it could, had the additional stages not been decoupled. The net result of this is a more efficient and flexible designed compressor. Additionally, with the increasing demand for products offering better energy efficiency, the compressor herein can be better optimized to provide improved load matching, capacity control and efficiency at multiple design points.
The invention described here enhances the compressor's ability to operate in wide ranging conditions with improved efficiency by way of allowing the skilled designer to select a configuration to achieve and optimize multiple specific design points within the same compressor by way of selecting how many impellers are required to meet the specific capacity and head requirement. Moreover, it provides a feed back loop and control system logic used to optimize the compressor's performance and determine when to switch to multiple compressor stages.
Although the present invention has been described hereinabove by way of specific embodiments thereof, it can be modified, without departing from the nature and teachings of the subject invention as defined in the appended claims.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB2008/003717 | 10/8/2008 | WO | 00 | 9/20/2010 |
Number | Date | Country | |
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60984466 | Nov 2007 | US |