Gas compressor

From Free net encyclopedia

A gas compressor is a mechanical device that increases the pressure of a gas by reducing its volume. Compression of a gas naturally increases its temperature.

Compressors are closely related to pumps: both increase the pressure on a fluid and both can transport the fluid through a pipe. As gases are compressible, the compressor also reduces the volume of a gas, whereas the main result of a pump raising the pressure of a liquid is to allow the liquid to be transported elsewhere.

Contents

Compressor designs

Image:Air compressor.jpg

Some important designs of compressors include:

  • Reciprocating compressors—uses pistons driven by a crankshaft. They are both stationary and portable, can be single or multi-staged, and can be driven by electric motors or internal combustion engines. Small reciprocating compressors from 5 to 30 HP are commonly seen in automotive applications and are typically for intermittent duty. Larger reciprocating compressors up to 1000 HP are still commonly found in large industrial applications, but their numbers are declining as they are replaced by less costly rotary screw compressors. Discharge pressures can range from low pressure to very high pressure (>5000 psi or 35 MPa).
  • Rotary screw compressors—uses two meshed rotating positive-displacement helical screws to force the gas into a smaller space. These are usually for continuous, commercial and industrial applications and are both stationary and portable. Their application can be from 5 hp (3.7 kW) to over 500 hp (375 kW) and from low pressure to very high pressure (>1200 psi or 8.3 MPa). They are commonly seen with roadside repair crews powering airtools. This type is also used for many automobile engine superchargers because it is easily matched to the induction capacity of a piston engine.
  • Centrifugal compressors—a vaned rotating disk or impeller in a shaped housing forces the gas to the rim of impeller increasing the velocity of the gas. A diffuser (divergent duct) section converts the velocity energy to pressure energy. These are used for continuous, heavy industrial uses and are usually stationary. Their application can be from 100 hp (75 kW) to thousands of horsepower. With multiple staging, they can achieve extremely high output pressures greater than 10,000 lbf/in² (69 MPa). Many large snow-making operations (like ski resorts) use this type of compressor. They are also used in internal combustion engines as superchargers and turbochargers. Centrifugal compressors are used in small gas turbine engines or as the final compression stage of medium sized gas turbines.
  • Axial-flow compressor—a series of fans spinning on a shaft in a tapered tube draw in gas at one end and, with the aid of interstage stators (a series of convergent and divergent ducts), compress it and output it at the other end. Usually for very high flow applications. Almost always multi-staged. Variable geometry often used to improve handling beyond about 4:1 design pressure ratio. Most common compressor in large gas turbine engines.
  • Diagonal or mixed-flow compressor —similar to a centrifugal compressor, but with a radial and axial velocity component at exit from the rotor. Diffuser is often used to turn diagonal flow to the axial direction. Lower diameter diffuser than equivalent CF compressor.
  • Scroll compressor—similar to a rotary screw device, this one includes two interleaved spiral-shaped scrolls to compress a gas. Its output is more pulsed than the latter and this factor has caused its declining industrial use. Can be found in automotive use as a supercharger.

Air compressors sold to and used by the general public are often attached on top of a tank for holding the pressurized air. Oil-lubricated and oil-free compressors are available.

Applications

Gas compressors are used in various applications where either higher pressures or lower volumes of gas are needed:

Temperature

Charles's law says "when a gas is compressed temperature is raised".

There are three possible relationships between temperature and pressure in a gas undergoing compression:

  • isothermal - gas at final stage of compression is same temperature as at beginning of compression. In this cycle, heat is removed at the same rate as it is added by the work of compression. This is impractical for a working machine.
  • adiabatic - This assumes that there is no heat transfer, into or out of the process, and that all work added is expended in creating a pressure rise. Theoretical temperature rise is T2 = T1·Rc((K-1)/K)), with T1 and T2 in degrees Rankine or kelvins, and K = ratio of specific heats (approximately 1.4 for air). The rise in air and temperature ratio means compression does not follow a simple pressure to volume ratio. This is less efficient, but quick.
  • Polytropic - This assumes that heat may enter or leave the process, and that work added can appear as both increased pressure (useful work) and increased temperature above adiabatic (losses due to cycle efficiency). Cycle efficiency is then the ratio of temperature rise at theoretic 100 percent (adiabatic) vs. actual (polytropic).

Staged compression

Since compression generates heat, the compressed air is to be cooled between stages making the compression less adiabatic and more isothermal. The inter-stage coolers cause condensation meaning water separators with drain valves are present. The compressor flywheel may drive a cooling fan.

For instance in a typical diving compressor, the air is compressed in three stages. If each stage has a compression ratio of 7 to 1, the compressor can output 343 times atmospheric pressure (7 x 7 x 7 = 343).

Prime movers

There are many options for the "prime mover" or motor which powers the compressor:

See also

de:Verdichter es:Compresor (máquina) fr:Compresseur mécanique id:Kompresor it:Compressore nl:Compressor (gas) ja:圧縮機 no:Kompressor pl:Sprężarka pt:Compressor sl:Kompresor sv:Kompressor