The present disclosure relates to a method and apparatus for enhancing compressor efficiency relates to economizers for compressors, particularly including screw compressors.
Compressors are used in various compression systems (e.g., refrigeration systems) to compress gas, such as freon, ammonia, natural gas, or the like, which is used to provide cooling capacity. One type of compressor is a single screw gas compressor, which is comprised of three basic components that rotate and complete the work of the compression process. These components include a single cylindrical main screw rotor with helical grooves, and two gate rotors (also known as star or star-shaped rotors), each gate rotor having a plurality of teeth. The rotational axes of the gate rotors are parallel to each other and mutually perpendicular to the axis of the main screw rotor. This type of compressor employs a housing in which the helical grooves of the main rotor mesh with the teeth of the gate rotors on opposite sides of the main rotor to define gas compression chambers. The housing is provided with two gas suction ports (one near each gate rotor) for inputting the gas and two gas discharge ports (one near each gate rotor) for entry and exit of the gas to the gas compression chambers. It is known to provide two dual slide valve assemblies on the housing (one assembly near each gate rotor) with each slide valve assembly comprising a suction valve (also referred to as a “capacity slide valve”) and a discharge slide valve (also referred to as a “volume slide valve”) for controlling an associated intake channel and an associated discharge channel, respectively. An electric motor imparts rotary motion through a driveshaft to the compressor's main rotor, which in turn rotates the two intermeshed gate rotors, compressing gas in the gas compression chambers. The compressed gas is passed to a condenser which converts the gas into a liquid. The liquid is further passed to an evaporator that converts the liquid into a gas again while providing cooling in the process.
To increase efficiency of a single screw compressor, an economizer, which is common in the industry, may be provided. The economizer function for screw compressors provides an increase in system capacity and efficiency by sub-cooling the liquid from the condenser through a heat exchanger or flash tank before it enters into the evaporator. More particularly, sub-cooling for the liquid is provided by sending high pressure liquid from the condenser into an economizer vessel through an expansion device to an intermediate pressure. The intermediate pressure in the economizer vessel is provided by an economizer port located part way in the compression cycle process of the screw compressor.
When the compressor unloads below about 60% of the full load capacity, the side/economizer port will drop in pressure level, ultimately being fully open to suction. Therefore, the liquid pressure decreases eventually down to suction pressure and no pressure difference will exist to push the liquid from the economizer vessel to the evaporator. Another side effect when the economizer port is fully opened to suction is the suction pressure will rise and the load on the compressor will need to be increased to keep the suction pressure constant.
One known method to maintain a constant economizer side port pressure is to keep the capacity slide position at 100% and run the compressor with a variable frequency drive (VFD), which can be used to unload the compressor by reducing the speed of the compressor instead of utilizing the capacity slide. Although this serves to maintain the desired pressure ratio at the economizer port, various drawbacks arise. For example, the added expense of purchasing the VFD and maintaining it is undesirable. In addition, the need for increased horsepower due to the inherent losses of the VFD can further increase cost by necessitating a larger capacity compressor. Further, the overall efficiency drops at lower speed due to the losses of the sealing effect between the internal bore and the threads of the rotor, which would allow additional gas to bypass from the high pressure side to the suction side of the compressor, and therefore increase operating costs.
Accordingly, it would be desirable to provide a method and apparatus for enhancing compressor efficiency that overcomes one or more of the aforementioned drawbacks.
In at least some embodiments, the method and apparatus for enhancing compressor efficient relates to a single screw gas compressor with a housing including a cylindrical bore; primary and secondary gate rotors mounted for rotation in the housing, each gate rotor having a plurality of gear teeth, a main rotor rotatably mounted in the bore and having a plurality of grooves and a plurality of threads, wherein each groove meshingly engages at least one of the gear teeth from each gate rotor a primary economizer port in communication with the cylindrical bore, and a secondary economizer port in communication with the cylindrical bore.
In at least some embodiments, the method and apparatus for enhancing compressor efficient relates to a cooling system including a compressor having: a housing including a cylindrical bore; a pair of gate rotors mounted for rotation in the housing, each gate rotor having a plurality of gear teeth; a main rotor rotatably mounted in the bore and having a plurality of grooves and a plurality of threads, wherein each groove meshingly engages at least one of the gear teeth from each gate rotor; a primary economizer port in communication with the cylindrical bore; and a secondary economizer port in communication with the cylindrical bore. The cooling system further including an economizer tank in communication with at least one of the primary economizer port and secondary economizer port, wherein the economizer tank provides pressurized refrigerant gas to the grooves via at least one of the primary economizer port and the secondary economizer port.
In at least some embodiments, the method and apparatus for enhancing compressor efficient relates to a method of enhancing compressor efficiency that includes receiving gas at suction ports of a compressor, rotating a main rotor inside a bore of the compressor, wherein the main rotor includes grooves and the bore includes a bore wall, compressing the gas received from the suction ports inside gas compression chambers formed by the grooves and the bore wall, receiving a first portion of gas at a first of the gas compression chambers through a primary economizer port during a high compressor load, and receiving a second portion of gas at a second of the gas compression chambers through a secondary economizer port during low compressor load.
Other embodiments, aspects, features, objectives and advantages of the method and apparatus for enhancing compressor efficiency will be understood and appreciated upon a full reading of the detailed description and the claims that follow.
Embodiments of the method and apparatus for enhancing compressor efficiency are disclosed with reference to the accompanying drawings and are for illustrative purposes only. The method and apparatus for enhancing compressor efficiency is not limited in its application to the details of construction or the arrangement of the components illustrated in the drawings. The method and apparatus for enhancing compressor efficiency is capable of other embodiments or of being practiced or carried out in other various ways. Like reference numerals are used to indicate like components. In the drawings:
Referring to
Referring to
Compressor housing 102 includes a cylindrical bore 128 in which main rotor 108 is rotatably mounted longitudinally therein. Main rotor 108, which is generally cylindrical and has a plurality of helical grooves 130 formed therein (for example, six grooves are illustrated) defining gas compression chambers 132, is provided with a rotor output shaft 134 (
The housing 102 includes spaces 144 wherein the primary and secondary gate rotors 110, 112 are rotatably mounted and located on opposite sides (i.e., 180 degrees apart) of the main rotor 108. Each of the gate rotors 110, 112 has a plurality of gear teeth 150 and is provided with a respective gate rotor shaft 152 which is rotatably supported at opposite ends on bearing assemblies 154 (
The compressor housing 102 is provided with a main suction port 159 (
Referring still to
Turning now to
With reference to
Referring to
With reference to
In general compressor operation, when a compressor is unloaded below about 60% of the compressor's full load capacity, the pressure at an economizer port drops to a level where the added efficiency of an economizer ceases to provide sufficient benefit. In the instant case, as the load capacity of the compressor 100 is reduced, via the capacity slides 114, 120 (based on a lower load demand), the gas pressure available at the primary economizer port 104 and the secondary economizer port 106 will be reduced. As the pressure at the primary economizer port 104 is reduced to equal the suction pressure at the primary suction port 159 (
The compressor 100 has been discussed above primarily with regard to the compressor function. To provide a more complete system overview,
As seen in
In addition to the aforementioned inter-connections, the economizer tank 204 further includes an economizer line 240 that passes gas refrigerant from the economizer tank 204 through an economizer output port 242 to a third expansion valve 244, and split into a primary economizer line 250 and secondary economizer line 252. The primary economizer line 250 is connected to the primary economizer port 104 through a primary shut-off valve 254. The secondary economizer line 252 is connected to the secondary economizer port 106 through a secondary shut-off valve 256.
Control of gas flow at the primary economizer port 104 is performed by the primary shut-off valve 254, while gas flow at the secondary economizer port 106 is controlled at the secondary shut-off valve 256. The primary shut-off valve 254 and secondary shut-off valve 256 are configured so that one valve is open while the other is closed, with the primary shut-off valve 254 being in an open position during high compressor load (about 60-100% load) and the secondary shut-off valve 256 being in an open position during low compressor load (about 10-59% load). The desired open/closed positions of these valves 244, 254 can be determined in response to feedback received from various sources, such as pre-determined set-points and limits, as well as active sensors monitoring the compressor 100 (e.g., loading status). Control of the valves 254, 256 can be performed by one or more of various components, using electrical, pneumatic, and/or mechanical methods. The percent of load that is considered to be a high compressor load and low compressor load can vary based on numerous criteria, such as compressor capacity, load conditions, etc., and as such should be considered exemplary ranges as various other ranges can be utilized as well.
During operation of the cooling system 200, under high compressor load conditions, the primary economizer port 104 is opened via the primary shut-off valve 254, thereby providing sufficient intermediate pressure at the economizer tank 204 to sub-cool the liquid in the economizer tank 204. When the load conditions are changed to a low compressor load, the primary shut-off valve 254 is closed and the secondary shut-off valve 256 is opened. The higher pressure available from the secondary economizer port 106 is then available to maintain the intermediate pressure at an acceptable level to sub-cool the liquid and push the liquid refrigerant to the evaporator 206. When the compressor is started under low compressor load conditions, the secondary shut-off valve 256 can be utilized first.
Although the figures are largely representative of a single screw compressor, the apparatus and method for enhancing compressor efficiency can be adapted for use with other compressor types. It is specifically intended that the method and apparatus for enhancing compressor efficiency not be limited to the embodiments and illustrations contained herein, but include modified forms of those embodiments including portions of the embodiments and combinations of elements of different embodiments as come within the scope of the following claims. In addition, the order of various steps of operation described herein can be varied. Further, numerical ranges provided herein are understood to be exemplary and shall include all possible numerical ranges situated therebetween.
This application claims the benefit under 35 U.S.C. Section 119(e) of U.S. Provisional Application No. 61/706,420 filed Sep. 27, 2012, the entire teachings and disclosures of which are incorporated herein by reference.
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