Part I of II…
The point of this two-part article is to alert the reader to the (often considerable) merits of twin-screw rotary compressors and to set the record straight on wet screw machines. For both dry screw and wet screw compressors, typical rotor profiles are shown in Fig. 1. These machines represent a sub-set of the machinery group making up rotating positive-displacement compressors. Of the various machines available, twin rotary screw compressors are used primarily in higher pressure air and process gas services, the subject of this article, whereas certain other rotary piston blowers and single-screw compressors are often used in lower pressure, high-volume applications. They are not covered here.
Rotating positive-displacement machines (like the one shown in Fig. 2) offer the same advantage as reciprocating positive-displacement equipment with regard to flow vs. pressure relationships, i.e., nearly constant inlet flow volume under varying discharge pressure conditions. Unlike centrifugal and axial machines, screw compressors do not have a surge limitation. Thus, there is no minimum throughput requirement for rotating positive displacement compressors.
The rotor tip speeds on rotary screw and rotary piston blowers are low; this allows for liquid injection or liquid flooding, which facilitates handling of contaminated gases. By design, the rotors are self-cleaning during operation, but contaminants must be kept away from the bearings. Likewise, dirt in the compression space has to be removed by filtration or other means.
Oil-free vs. oil-flooded models
Rotary screw compressors are available in oil-free or oilflooded construction. Technically speaking, oil-free refers to not having oil in the compression space, but bearings still require lubrication by a clean medium. This lubricant is typically clean oil, although clean pressurized water can also be used [Ref. 1]. In fact, while pressurized water represents less well-known advanced technology, it has nevertheless been applied for decades. In the hands of truly competent compressor manufacturers, water-flooded screw compressors have been remarkably effective and successful in some of the dirtiest services [Ref. 1].
While oil-free twin-screw compressors are widely called dry screw machines, at least one prominent manufacturer defines and designates as “dry screw” any screw compressor equipped with timing gears. Therefore, whether the compression space is dry, oil-flooded or water-injected makes no difference: With timing gears keeping the two screws synchronized, it should be labeled a dry screw machine. Without timing gears, it cannot function as a dry screw machine, because the resulting contact of mating rotors would destroy the machine. If there are no timing gears, a separating liquid must be used. Any separating liquid circulating in the compression space will make it a wet screw machine [Ref. 2].
Fields of application for oil-free machines include all processes that cannot tolerate contamination of the compressed gas or where the lubricating oil would be contaminated by the gas. Oil-flooded machines can achieve slightly higher efficiencies than “dry screw” machines and can utilize the oil for cooling as well [Ref. 3]. The same statements could be made for water-flooded machines. In some instances, the bearing lube circuit must be totally separate from the fluid circuit used in the compression space. Whenever this requirement is disregarded, the purchaser/user may end up with either high maintenance costs or low equipment reliability.
Properly designed rotary screw compressors are constructed with no metallic contact whatsoever inside the compression chambers, either between the rotors themselves or between these and the walls of the housing. Although originally intended for air compression, rotary screw compressors are now found in numerous services in the petrochemical and related industries. These include air separation plants, industrial refrigeration plants, evaporation plants, mining and metallurgical plants.
Practically all gases can be compressed: ammonia, argon, ethylene, acetylene, butadiene, chlorine gas, hydrochloric gas, natural gas, flare gas, blast furnace gas, swamp gas, helium, lime-kiln gas, coking-plant gas and carbon monoxide gas can be compressed with screw machines. The same is true for all hydrocarbon combinations; town gas, air/methane gas, propane, propylene, flue gas, crude gas, sulfur dioxide, oxide of nitrogen, nitrogen, styrene gas, vinyl chloride gas and hydrogen gas can be found on the reference tabulations of experienced manufacturers.
One manufacturer alone has at least 20 oil-flooded twinscrew compressors in successful service with three years between shutdowns. While process conditions vary widely, there are perhaps several manufacturers with similar experience. Their compressors may not be lowest installed cost, but they usually represent best value and lowest possible life cycle cost by wide margins.
Application limits for rotary screw compressors are set by the pressure and temperature ranges and by the maximum allowable speeds of the machines. Oil-free rotary screw compressors can be mechanically loaded with pressure differences up to 12 bar, and oil-flooded compressors up to 20 bar. Higher pressure differences are possible in special cases. Flow volumes up to 60,000 m3/hr (~35,000 acfm) have been accommodated in these compressors.
The maximum allowable compression ratio for one twin-screw compressor stage is that which will not cause the final compression temperature to rise above the permitted value of 250 C (482 F). This compression ratio and the associated temperature will to a very large extent depend on the specific heat ratio (cP/cV) of the gas to be compressed. For example, where the specific heat ratio (cP/cV) equals 1.4, the maximum compression ratio would be approximately 4.5, and where the specific heat ratio (cP/cV) equals 1.2, the maximum compression ratio would be approximately 10 for an oil-free twin-screw compressor stage.
Multistage (multi-casing) arrangements are not uncommon and can result in pressure ranges from approximately 0.1 bar absolute to 40 bar. Even 100 bar has been reached in some instances. Interstage cooling is used in many of these applications. Depending on compressor size, speeds from 2000 to 20,000 rpm can be encountered. The limiting factor is often the circumferential speed of the male rotor, which typically ranges from 40 to approximately 120 m/sec, and up to a maximum of 150 m/sec for very light gases.
In principle, it is necessary to consider the volume-control options for dry-running and for oil-injection-type screw compressors separately.
Controlling dry screw compressors…
Controlling oil-injected screw compressors…
Coming in Part II
The concluding installment in this series will discuss oilfree vs. oil-flooded rotary screw compressors and available seal design options.
1. Bloch, Heinz P., A Practical Guide to Compressor Technology, (2nd Edition, 2006) John Wiley & Sons, (ISBN 0-471-727930-8). [See also 1st Spanish Edition, (1998) McGraw-Hill, New York and Mexico City, ISBN 970-10- 1825-7].
2. Bloch, Heinz P., and Noack, Pierre, “Recent Experience With Large Liquid-Injected Rotary Screw Process Gas Compressors,” (Proceedings of 20th Turbomachinery Symposium, Texas A & M University, Dallas, TX).
3. Bloch, Heinz P., and Soares, Claire, Process Plant Machinery, 2nd Edition, 1998, Elsevier Publishing, London-New York-Amsterdam, ISBN 0-7506-7081-9.