View source for Compressor

{{Short description|Machine to increase pressure of gas by reducing its volume}}
{{other uses}}
[[File:Small stationary Bauer HP compressor installation DSC09403.JPG|thumb|A small stationary high pressure breathing air compressor for filling scuba cylinders]]
[[File:Atlas Copco XASS - Ystad-2024.jpg|thumb|A powerful compressor for street work. Model XASS from [[Atlas Copco]] circa 1985.]]
[[File:Gas Compressor wellsite.jpg|thumb|right|Natural gas compressor at a gas well]]
[[File:High pressure compressor BellisMorcom.jpg|thumb|right|High pressure reciprocating compressor from Belliss and Morcom, used in the bottling industry]]
A '''compressor''' is a mechanical device that increases the [[pressure]] of a [[gas]] by reducing its [[volume]]. An [[air compressor]] is a specific type of gas compressor.

Many compressors can be staged, that is, the gas is compressed several times in steps or stages, to increase discharge pressure. Often, the second stage is physically smaller than the primary stage, to accommodate the already compressed gas without reducing its pressure. Each stage further compresses the gas and increases its pressure and also temperature (if inter cooling between stages is not used).

==Types==
Compressors are similar to [[pump]]s: both increase the pressure on a [[fluid]] (such as a gas) and both can transport the fluid through a [[pipe (material)|pipe]]. The main distinction is that the focus of a compressor is to change the density or volume of the fluid, which is mostly only achievable on gases. Gases are compressible, while liquids are relatively incompressible, so compressors are rarely used for liquids. The main action of a pump is to pressurize and transport liquids.

The main and important types of gas compressors are illustrated and discussed below:
[[File:Gas-compressors-types-yed.png|frame|center]]

===Positive displacement===
A positive displacement compressor is a system that compresses the air by the displacement of a mechanical linkage reducing the volume (since the reduction in volume due to a piston in thermodynamics is considered as positive displacement of the piston).{{vague|date=May 2018}}

Put another way, a positive displacement compressor is one that operates by drawing in a discrete volume of gas from its inlet then forcing that gas to exit via the compressor's outlet.  The increase in the pressure of the gas is due, at least in part, to the compressor pumping it at a mass flow rate which cannot pass through the outlet at the lower pressure and density of the inlet.

====Reciprocating compressors====

{{main|Reciprocating compressor}}
[[File:ReciprocatingCompressor.jpg|right|thumb|A motor-driven six-cylinder reciprocating compressor that can operate with two, four or six cylinders.]]
'''Reciprocating compressors''' use [[piston]]s driven by a crankshaft. They can be either stationary or portable, can be single or multi-staged, and can be driven by electric motors or internal combustion engines.<ref name=Perry /><ref>{{cite book
  |author1=Bloch, H.P. 
  |author2=Hoefner, J.J.
  |title=Reciprocating Compressors, Operation and Maintenance
  |publisher=Gulf Professional Publishing
  |year=1996
  |isbn=0-88415-525-0
}}</ref><ref>[http://www.machinerylubrication.com/article_detail.asp?articleid=775&pagetitle=Reciprocating%20Compressor%20Basics Reciprocating Compressor Basics] {{webarchive|url=https://web.archive.org/web/20090418034216/http://www.machinerylubrication.com/article_detail.asp?articleid=775&pagetitle=Reciprocating%20Compressor%20Basics |date=2009-04-18 }} Adam Davis, Noria Corporation, ''Machinery Lubrication'', July 2005</ref> Small reciprocating compressors from 5 to 30&nbsp;[[horsepower]] (hp) are commonly seen in automotive applications and are typically for intermittent duty. Larger reciprocating compressors well over {{convert|1000|hp|abbr=on}} are commonly found in large industrial and petroleum applications. [[Discharge pressure]]s can range from low pressure to very high pressure (>18000 psi or 124 MPa). In certain applications, such as air compression, multi-stage double-acting compressors are said to be the most efficient compressors available, and are typically larger, and more costly than comparable rotary units.<ref>{{Cite web|url=https://www.thomasnet.com/articles/machinery-tools-supplies/|archive-url=https://web.archive.org/web/20100428012223/http://www.thomasnet.com/articles/machinery-tools-supplies/industrial-compressed-air-systems|url-status=dead|title=Machinery, Tools & Supplies Articles on ThomasNet|archive-date=April 28, 2010|website=www.thomasnet.com}}</ref> Another type of reciprocating compressor, usually employed in automotive cabin [[air conditioning]] systems,{{citation needed|date=August 2017}} is the swash plate or wobble plate compressor, which uses pistons moved by a swash plate mounted on a shaft (see ''[[axial piston pump]]'').

Household, home workshop, and smaller job site compressors are typically reciprocating compressors {{cvt|1.5|hp}} or less with an attached receiver tank.

A [[linear compressor]] is a reciprocating compressor with the piston being the rotor of a linear motor.

This type of compressor can compress a wide range of gases, including refrigerant, hydrogen, and natural gas. Because of this, it finds use in a wide range of applications in many different industries and can be designed to a wide range of capacities, by varying size, number of cylinders, and cylinder unloading. However, it suffers from higher losses due to clearance volumes, resistance due to discharge and suction valves, weighs more, is difficult to maintain due to having a large number of moving parts, and it has inherent vibration.<ref name="autogenerated1">{{Cite web |title=Ref Doc |url=https://download.schneider-electric.com/files?p_Doc_Ref=SPD_VAVR-AE7T7G_EN |website=download.schneider-electric.com}}</ref>

====Ionic liquid piston compressor====

{{main|Ionic liquid piston compressor}}
An [[ionic liquid piston compressor]], ''ionic compressor'' or ''ionic liquid piston pump'' is a [[hydrogen compressor]] based on an [[ionic liquid]] piston instead of a metal piston as in a piston-metal [[diaphragm compressor]].

====Rotary screw compressors====

[[File:RotaryScrewCompressor.gif|thumb|a Diagram of a rotary screw compressor|alt=www]]
{{main|Rotary screw compressor}}
'''Rotary screw compressors''' use two meshed rotating positive-displacement [[Helix|helical screws]] to force the gas into a smaller space.<ref name=Perry/><ref>[http://www.blackmer.com/tech-screw.jsp Screw Compressor] {{webarchive|url=https://web.archive.org/web/20080110103341/http://www.blackmer.com/tech-screw.jsp |date=2008-01-10 }} Describes how screw compressors work and include photographs.</ref><ref>[http://www.domnickhunter.com/tech_Centre.asp?chapter=1&section=3_Screw-Compressors_2_3.htm&getIndex=false Technical Centre] {{webarchive|url=https://web.archive.org/web/20071213211548/http://www.domnickhunter.com/tech_Centre.asp?chapter=1&section=3_Screw-Compressors_2_3.htm&getIndex=false |date=2007-12-13 }} Discusses oil-flooded screw compressors including a complete system flow diagram</ref> These are usually used for continuous operation in commercial and industrial applications and may be either stationary or portable. Their application can be from {{convert|3|hp|kW}} to over {{convert|1200|hp|kW}} and from low pressure to moderately high pressure (>{{convert|1200|psi|MPa|1|abbr=on|disp=or}}).

The classifications of rotary screw compressors vary based on stages, cooling methods, and drive types among others.<ref>{{Cite news|url=http://www.industrialcompressorsolutions.com/articles/how-does-a-rotary-screw-air-compressor-work|title=How Does a Rotary Screw Air Compressor Work?|last=ICS|access-date=2017-08-16|language=en|url-status=live|archive-url=https://web.archive.org/web/20170817001135/http://www.industrialcompressorsolutions.com/articles/how-does-a-rotary-screw-air-compressor-work|archive-date=2017-08-17}}</ref> Rotary screw compressors are commercially produced in Oil Flooded, Water Flooded and Dry type. The efficiency of rotary compressors depends on the air drier,{{clarify|date=May 2014}} and the selection of air drier is always 1.5 times volumetric delivery of the compressor.<ref>{{Cite book|url=https://books.google.com/books?id=1w5yBgAAQBAJ&q=%22The+efficiency+of+rotary+compressors+depends+on+the+air+drier%22&pg=PA643|title=Hydraulic Fracturing Operations: Handbook of Environmental Management Practices|last1=Cheremisinoff|first1=Nicholas P.|last2=Davletshin|first2=Anton|date=2015-01-28|publisher=John Wiley & Sons|isbn=9781119100003|language=en|url-status=live|archive-url=https://web.archive.org/web/20171224222642/https://books.google.com/books?id=1w5yBgAAQBAJ&pg=PA643&lpg=PA643&dq=%22The+efficiency+of+rotary+compressors+depends+on+the+air+drier%22&source=bl&ots=DIZJEjhMaW&sig=coZe1GEy2bN8CTUmSaK8IuA3jSw&hl=en&sa=X&ved=0ahUKEwjV9YOjntzVAhUp7oMKHeIvCLoQ6AEILDAB#v=onepage&q=%22The%20efficiency%20of%20rotary%20compressors%20depends%20on%20the%20air%20drier%22&f=false|archive-date=2017-12-24}}</ref>

Designs with a single screw<ref>{{cite web|url=https://www.daikinapplied.uk/features/single-screw-compressor |title=Single Screw Compressor |website=Daikin Applied UK}}</ref> or three screws<ref>{{citation|url=http://docs.lib.purdue.edu/cgi/viewcontent.cgi?article=2824&context=icec |last=Jacobs |first=John S. |title=Variable Speed Tri-Rotor Screw Compression Technology |date=2006 |publisher=International Compressor Engineering Conference. Paper 1825.}}</ref> instead of two exist.

Screw compressors have fewer moving components, larger capacity, less vibration and surging, can operate at variable speeds, and typically have higher efficiency. Small sizes or low rotor speeds are not practical due to inherent leaks caused by clearance between the compression cavities or screws and compressor housing.<ref name=autogenerated1 /> They depend on fine machining tolerances to avoid high leakage losses and are prone to damage if operated incorrectly or poorly serviced.

====Rotary vane compressors====

[[Image:Rotary vane pump.svg|thumb|300px|Eccentric rotary-vane pump]]
{{See also|Rotary vane pump}}
'''Rotary vane compressors''' consist of a rotor with a number of blades inserted in radial slots in the rotor. The rotor is mounted offset in a larger housing that is either circular or a more complex shape. As the rotor turns, blades slide in and out of the slots keeping contact with the outer wall of the housing.<ref name=Perry/> Thus, a series of increasing and decreasing volumes is created by the rotating blades. Rotary vane compressors are, with piston compressors one of the oldest of compressor technologies.

With suitable port connections, the devices may be either a compressor or a vacuum pump. They can be either stationary or portable, can be single or multi-staged, and can be driven by electric motors or internal combustion engines. Dry vane machines are used at relatively low pressures (e.g., {{convert|2|bar|kPa psi|abbr=on|disp=or}}) for bulk material movement while oil-injected machines have the necessary volumetric efficiency to achieve pressures up to about {{convert|13|bar|kPa psi|abbr=on}} in a single stage. A rotary vane compressor is well suited to electric motor drive and is significantly quieter in operation than the equivalent piston compressor.

Rotary vane compressors can have mechanical efficiencies of about 90%.<ref>{{Cite web|url=http://www.matteicomp.com/|archive-url=https://web.archive.org/web/20100509233715/http://www.matteicomp.com/compressor-news.htm?id=165176063|url-status=dead|title=Rotary Vane Compressors and the Vane Compressor - Compressors for stationary industrial and OEM applications - Mattei|first=Mattei Compressors|last=Inc|archive-date=May 9, 2010|website=www.matteicomp.com}}</ref>

====Rolling piston====

[[File:Rollkolbenverdichter.png|thumb|Rolling piston compressor]]
The Rolling piston in a rolling piston style compressor plays the part of a partition between the vane and the rotor.<ref>{{cite web|url=http://docs.lib.purdue.edu/cgi/viewcontent.cgi?article=1390&context=icec|title=Motion of Rolling Piston in Rotary Compressor|website=Purdue University|archive-url=https://web.archive.org/web/20170816232859/http://docs.lib.purdue.edu/cgi/viewcontent.cgi?article=1390&context=icec|archive-date=2017-08-16|url-status=live|access-date=2017-08-16}}</ref> Rolling piston forces gas against a stationary vane.

2 of these compressors can be mounted on the same shaft to increase capacity and reduce vibration and noise.<ref>{{Cite web|url=https://news.samsung.com/global/what-the-new-samsung-mini-rotary-compressor-means|title=What the New Samsung Mini Rotary Compressor Means|website=news.samsung.com}}</ref> A design without a spring is known as a swing compressor.<ref>{{Cite web|url=https://www.daikin.com/products/ac/lineup/skyair/|title=High Efficiency Compressor to Achieve a High COP {{pipe}} Air Conditioning and Refrigeration {{pipe}} Daikin Global|website=www.daikin.com}}</ref>

In refrigeration and air conditioning, this type of compressor is also known as a rotary compressor, with rotary screw compressors being also known simply as screw compressors.

It offers higher efficiency than reciprocating compressors due to less losses from the clearance volume between the piston and the compressor casing, it's 40% to 50% smaller and lighter for a given capacity (which can impact material and shipping costs when used in a product), causes less vibration, has fewer components and is more reliable than a reciprocating compressor. But its structure does not allow capacities beyond 5 refrigeration tons, is less reliable than other compressor types, and is less efficient than other compressor types due to losses from the clearance volume.<ref name="autogenerated1"/>

====Scroll compressors====

[[File:Two moving spirals scroll pump.gif|thumb|right|Mechanism of a scroll pump]]
{{Main|Scroll compressor}}
A '''scroll compressor''', also known as '''scroll pump''' and '''scroll vacuum pump''', uses two interleaved spiral-like vanes to [[pump]] or compress [[fluid]]s such as [[liquids]] and [[gas]]es. The vane geometry may be [[involute]], [[archimedean spiral]], or hybrid curves.<ref>Tischer, J., Utter, R: "Scroll Machine Using Discharge Pressure For Axial Sealing," U.S. Patent 4522575, 1985.</ref><ref>Caillat, J., Weatherston, R., Bush, J: "Scroll-Type Machine With Axially Compliant Mounting," U.S. Patent 4767293, 1988.</ref><ref>Richardson, Jr., Hubert: "Scroll Compressor With Orbiting Scroll Member Biased By Oil Pressure," U.S. Patent 4875838, 1989.</ref> They operate more smoothly, quietly, and reliably than other types of compressors in the lower volume range.

Often, one of the scrolls is fixed, while the other orbits eccentrically without rotating, thereby trapping and pumping or compressing pockets of fluid between the scrolls.

Due to minimum clearance volume between the fixed scroll and the orbiting scroll, these compressors have a very high [[volumetric efficiency]].

These compressors are extensively used in air conditioning and refrigeration because they are lighter, smaller and have fewer moving parts than reciprocating compressors and they are also more reliable. They are more expensive though, so peltier coolers or rotary and reciprocating compressors may be used in applications where cost is the most important or one of the most important factors to consider when designing a refrigeration or air conditioning system.

This type of compressor was used as the [[G-Lader|supercharger]] on Volkswagen G60 and G40 engines in the early 1990s.

When compared with reciprocating and rolling piston compressors, scroll compressors are more reliable since they have fewer components and have a simpler structure, are more efficient since they have no clearance volume nor valves, and possess the advantages both of surging less and not vibrating so much. But, when compared with screw and centrifugal compressors, scroll compressors have lower efficiencies and smaller capacities.<ref name="autogenerated1"/>

====Diaphragm compressors====

{{main|Diaphragm compressor}}
A '''diaphragm compressor''' (also known as a '''membrane compressor''') is a variant of the conventional reciprocating compressor. The compression of gas occurs by the movement of a flexible membrane, instead of an intake element. The back-and-forth movement of the membrane is driven by a rod and a crankshaft mechanism. Only the membrane and the compressor box come in contact with the gas being compressed.<ref name=Perry/>

The degree of flexing and the material constituting the diaphragm affects the maintenance life of the equipment. Generally stiff metal diaphragms may only displace a few cubic centimeters of volume because the metal cannot endure large degrees of flexing without cracking, but the stiffness of a metal diaphragm allows it to pump at high pressures. Rubber or silicone diaphragms are capable of enduring deep pumping strokes of very high flexion, but their low strength limits their use to low-pressure applications, and they need to be replaced as plastic embrittlement occurs.

Diaphragm compressors are used for hydrogen and compressed natural gas ([[Compressed natural gas|CNG]]) as well as in a number of other applications.

[[File:DiaphragmCompressor.jpg|thumb|right|A three-stage diaphragm compressor]]
The photograph on the right depicts a three-stage diaphragm compressor used to compress hydrogen gas to {{convert|6000|psi|MPa|abbr=on}} for use in a prototype [[compressed hydrogen]] and [[compressed natural gas]] (CNG) fueling station built in downtown [[Phoenix, Arizona]] by the [[Arizona Public Service]] company (an electric utilities company). [[Reciprocating compressor]]s were used to compress the [[natural gas]]. The reciprocating natural gas compressor was developed by [[Sertco]].<ref>{{cite journal | author=Eric Slack | title=Sertco | date=Winter 2016 | url=http://www.emi-magazine.com/index.php/featured-content/1067-sertco | publisher=Phoenix Media Corporation | journal=Energy and Mining International | access-date=February 27, 2016 | url-status=live | archive-url=https://web.archive.org/web/20160304170914/http://www.emi-magazine.com/index.php/featured-content/1067-sertco | archive-date=March 4, 2016 }}</ref>

The prototype [[alternative fuel]]ing station was built in compliance with all of the prevailing safety, environmental and building codes in Phoenix to demonstrate that such fueling stations could be built in urban areas.

===Dynamic===
====Air bubble compressor====
Also known as a [[trompe]]. A mixture of air and water generated through turbulence is allowed to fall into a subterranean chamber where the air separates from the water. The weight of falling water compresses the air in the top of the chamber. A submerged outlet from the chamber allows water to flow to the surface at a lower height than the intake. An outlet in the roof of the chamber supplies the compressed air to the surface. A facility on this principle was built on the [[Montreal River (Timiskaming District)|Montreal River]] at Ragged Shutes near [[Cobalt, Ontario]] in 1910 and supplied 5,000 horsepower to nearby mines.<ref>{{cite journal|last=Maynard|first=Frank|date=November 1910|title=Five thousand horsepower from air bubbles|journal=Popular Mechanics|page=633|url=https://books.google.com/books?id=-N0DAAAAMBAJ|url-status=live|archive-url=https://web.archive.org/web/20170326071901/https://books.google.com/books?id=-N0DAAAAMBAJ&printsec=frontcover|archive-date=2017-03-26}}</ref>

====Centrifugal compressors====
[[File:CentrifugalCompressor.jpg|thumb|right|A single stage centrifugal compressor]]
[[File:Fan, before 1945.jpg|thumb|right|A single stage centrifugal compressor, early 1900s, G. Schiele & Co., Frankfurt am Main]]
{{main|Centrifugal compressor}}
'''Centrifugal compressors''' use a rotating disk or [[impeller]] in a shaped housing to force the gas to the rim of the impeller, increasing the velocity of the gas. A diffuser (divergent duct) section converts the velocity energy to pressure energy. They are primarily used for continuous, stationary service in industries such as [[oil refinery|oil refineries]], [[chemical plant|chemical]] and [[petrochemical]] plants and [[natural gas processing]] plants.<ref name=Perry >{{cite book
  |editor1=Perry, R.H. 
  |editor2=Green, D.W. 
  |title=[[Perry's Chemical Engineers' Handbook]]
  |edition=8th|publisher=McGraw Hill
  |year=2007
  |isbn=978-0-07-142294-9
}}</ref><ref>{{cite book|author=Dixon S.L.
  |title=Fluid Mechanics, Thermodynamics of Turbomachinery
  |edition=Third
  |publisher=Pergamon Press
  |year=1978|isbn=0-08-022722-8
}}</ref><ref>{{cite book
  |author=Aungier, Ronald H.
  |title=Centrifugal Compressors A Strategy for Aerodynamic design and Analysis
  |publisher=[[ASME]] Press
  |year=2000
  |isbn=0-7918-0093-8
}}</ref> Their application can be from {{convert|100|hp|kW}} to thousands of horsepower. With multiple staging, they can achieve high output pressures greater than {{convert|1000|psi|MPa|abbr=on}}.

This type of compressor, along with screw compressors, are extensively used in large refrigeration and air conditioning systems. Magnetic bearing (magnetically levitated) and air bearing centrifugal compressors exist.

Many large [[snowmaking]] operations (like [[ski resorts]]) use this type of compressor. They are also used in internal combustion engines as [[supercharger]]s and [[turbocharger]]s. Centrifugal compressors are used in small [[gas turbine]] [[engine]]s or as the final compression stage of medium-sized gas turbines.

Centrifugal compressors are the largest available compressors, offer higher efficiencies under partial loads, may be oil-free when using air or magnetic bearings which increases the heat transfer coefficient in evaporators and condensers, weigh up to 90% less and occupy 50% less space than reciprocating compressors, are reliable and cost less to maintain since less components are exposed to wear, and only generate minimal vibration. But, their initial cost is higher, require highly precise [[CNC]] machining, the impeller needs to rotate at high speeds making small compressors impractical, and surging becomes more likely.<ref name=autogenerated1 /> Surging is gas flow reversal, meaning that the gas goes from the discharge to the suction side, which can cause serious damage, specially in the compressor bearings and its drive shaft. It is caused by a pressure on the discharge side that is higher than the output pressure of the compressor. This can cause gases to flow back and forth between the compressor and whatever is connected to its discharge line, causing oscillations.<ref name="autogenerated1"/>

====Diagonal or mixed-flow compressors====
'''Diagonal''' or '''[[mixed-flow compressor]]s''' are similar to centrifugal compressors, but have a radial and axial velocity component at the exit from the rotor. The diffuser is often used to turn diagonal flow to an axial rather than radial direction.<ref>{{Cite book|url=https://books.google.com/books?id=WQcEDAAAQBAJ&q=diffuser+turns+diagonal+flow+to+axial+flow&pg=PT251|title=Pollution Control Handbook for Oil and Gas Engineering|last=Cheremisinoff|first=Nicholas P.|date=2016-04-20|publisher=John Wiley & Sons|isbn=9781119117889|language=en|url-status=live|archive-url=https://web.archive.org/web/20171224222642/https://books.google.com/books?id=WQcEDAAAQBAJ&pg=PT251&lpg=PT251&dq=diffuser+turns+diagonal+flow+to+axial+flow&source=bl&ots=rkZptfuirh&sig=RgvJpyW13dPTS677R4UWIOCaQtU&hl=en&sa=X&ved=0ahUKEwjbvIKZ9NnVAhXD6YMKHWfvCuwQ6AEINzAG#v=onepage&q=diffuser%20turns%20diagonal%20flo&f=false|archive-date=2017-12-24}}</ref> Comparative to the conventional centrifugal compressor (of the same stage pressure ratio), the value of the speed of the mixed flow compressor is 1.5 times larger.<ref>{{cite web|url=http://turbolab.tamu.edu/proc/turboproc/T13/T13139-147.pdf|title=Development of High Specific Speed Mixed Flow Compressors|last=Kano|first=Fumikata|website=Texas A&M University|archive-url=https://web.archive.org/web/20140811093700/http://turbolab.tamu.edu/proc/turboproc/T13/T13139%2D147.pdf|archive-date=2014-08-11|url-status=dead|access-date=2017-08-16}}</ref>

====Axial compressors====
[[File:Axial compressor.gif|thumb|right|An animation of an axial compressor.]]
{{main|Axial compressor}}
'''Axial compressors''' are dynamic rotating compressors that use arrays of fan-like [[airfoil]]s to progressively compress a fluid. They are used where high flow rates or a compact design are required.

The arrays of airfoils are set in rows, usually as pairs: one rotating and one stationary. The rotating airfoils, also known as blades or ''rotors'', accelerate the fluid. The stationary airfoils, also known as ''stators'' or vanes, decelerate and redirect the flow direction of the fluid, preparing it for the rotor blades of the next stage.<ref name=Perry /> Axial compressors are almost always multi-staged, with the cross-sectional area of the gas passage diminishing along the compressor to maintain an optimum axial [[Mach number]]. Beyond about 5 stages or a 4:1 design pressure ratio a compressor will not function unless fitted with features such as stationary vanes with variable angles (known as variable inlet guide vanes and variable stators), the ability to allow some air to escape part-way along the compressor (known as interstage bleed) and being split into more than one rotating assembly (known as twin spools, for example).

Axial compressors can have high efficiencies; around 90% [[polytropic]] at their design conditions. However, they are relatively expensive, requiring a large number of components, tight tolerances and high quality materials. Axial compressors are used in medium to large [[gas turbine]] engines, natural gas pumping stations, and some chemical plants.

==={{Anchor|Hermetically-sealed compressor}} Hermetically sealed, open, or semi-hermetic===
[[File:Lednička Zanussi ZRA 319 SW, kompresor s odpařovací miskou (002).JPG|thumb|A small hermetically sealed compressor in a common consumer [[refrigerator]] or [[freezer]] typically has a rounded steel outer shell permanently welded shut, which seals operating gases inside the system, in this case an [[Isobutane|R600a]] [[List of refrigerants|refrigerant]]. There is no route for gases to leak, such as around motor shaft seals. On this model, the plastic top section is part of an [[auto-defrost]] system that uses motor heat to evaporate the water.]]

Compressors used in [[Vapor-compression refrigeration|refrigeration]] systems must exhibit near-zero leakage to avoid the loss of the [[refrigerant]] if they are to function for years without service. This necessitates the use of very effective seals, or even the elimination of all seals and openings to form a [[Hermetic seal|hermetic]] system. These compressors are often described as being either '''hermetic''', '''open''', or '''semi-hermetic''', to describe how the compressor is enclosed and how the [[Electric motor|motor]] drive is situated in relation to the gas or vapor being compressed. Some compressors outside of refrigeration service may also be hermetically sealed to some extent, typically when handling toxic, polluting, or expensive gasses, with most non-refrigeration applications being in the petrochemical industry.

In hermetic and most semi-hermetic compressors, the compressor and motor driving the compressor are integrated, and operate within the pressurized gas envelope of the system. The motor is designed to operate in, and be cooled by, the refrigerant gas being compressed. Open compressors have an external motor driving a shaft that passes through the body of the compressor and rely on rotary seals around the shaft to retain the internal pressure.

The difference between the hermetic and semi-hermetic, is that the hermetic uses a one-piece welded steel casing that cannot be opened for repair; if the hermetic fails it is simply replaced with an entire new unit. A semi-hermetic uses a large cast metal shell with gasketed covers with screws that can be opened to replace motor and compressor components. The primary advantage of a hermetic and semi-hermetic is that there is no route for the gas to leak out of the system. The main advantages of open compressors is that they can be driven by any motive power source, allowing the most appropriate motor to be selected for the application, or even non-electric power sources such as an [[internal combustion engine]] or steam [[turbine]], and secondly the motor of an open compressor can be serviced without opening any part of the refrigerant system.

An open pressurized system such as an automobile air conditioner can be more susceptible to leak its operating gases. Open systems rely on lubricant in the system to splash on pump components and seals. If it is not operated frequently enough, the lubricant on the seals slowly evaporates, and then the seals begin to leak until the system is no longer functional and must be recharged. By comparison, a hermetic or semi-hermetic system can sit unused for years, and can usually be started up again at any time without requiring maintenance or experiencing any loss of system pressure. Even well lubricated seals will leak a small amount of gas over time, particularly if the refrigeration gasses are soluble in the lubricating oil, but if the seals are well manufactured and maintained this loss is very low.

The disadvantage of hermetic compressors is that the motor drive cannot be repaired or maintained, and the entire compressor must be replaced if a motor fails. A further disadvantage is that burnt-out windings can contaminate the whole systems, thereby requiring the system to be entirely pumped down and the gas replaced (This can also happen in semi hermetic compressors where the motor operates in the refrigerant). Typically, hermetic compressors are used in low-cost factory-assembled consumer goods where the cost of repair and labor is high compared to the value of the device, and it would be more economical to just purchase a new device or compressor. Semi-hermetic compressors are used in mid-sized to large refrigeration and air conditioning systems, where it is cheaper to repair and/or refurbish the compressor compared to the price of a new one. A hermetic compressor is simpler and cheaper to build than a semi-hermetic or open compressor.

==Thermodynamics of gas compression==

===Isentropic compressor===
A compressor can be idealized as internally reversible and [[adiabatic]], thus an [[isentropic]] steady state device, meaning the change in [[entropy]] is 0.<ref name="Cengel, Yunus A. 2012">Cengel, Yunus A., and Michaeul A. Boles. Thermodynamics: An Engineering Approach. 7th Edition ed. New York: Mcgraw-Hill, 2012. Print.</ref> 

The enthalpy change for a flow process can be calculated.<ref>{{cite web |last1=Alvi |title=TdS Equations |url=https://web1.eng.famu.fsu.edu/~alvi/EML3015/Lecture-notes/lecture%20notes/entropy%20change/tsld004.htm |website=Florida State University |publisher=Famu |access-date=1 February 2023}}</ref>

dH = VdP +TdS

Isentropic dS is zero.

dH = VdP

Non flow isentropic processes like some positive displacement compressors may use a different equation.<ref>{{cite web |last1=Mae |title=Non-Flow Thermodynamic Processes |url=http://wwwcourses.sens.buffalo.edu/mae431/ES12Ch04.pdf |website=courses.sens |publisher=buffalo.edu |access-date=2 February 2023}}</ref>

dH = PdV 

By defining the compression cycle as [[isentropic]], an ideal efficiency for the process can be attained, and the ideal compressor performance can be compared to the actual performance of the machine. Isotropic Compression as used in [[ASME]] PTC 10 Code refers to a reversible, adiabatic compression process<ref name="PTC 10 - Compressors and Exhauters">{{Cite web|url=https://www.asme.org/codes-standards/find-codes-standards/ptc-10-performance-test-code-compressors-exhausters|archive-url=https://web.archive.org/web/20150619013643/https://www.asme.org/products/codes-standards/ptc-10-1997-performance-test-code-compressors|url-status=dead|title=PTC-10 Performance Test Code on Compressors & Exhausters - ASME|archive-date=June 19, 2015|website=www.asme.org}}</ref>

Isentropic efficiency of Compressors:
: <math> \eta _C = \frac{\rm Isentropic \;Compressor\;Work}{\rm Actual\;Compressor\; Work}=\frac{W_s}{W_a} \cong \frac{h_{2s}-h_1}{h_{2a}-h_1}  </math>

: <math> h_1 </math> is the [[enthalpy]] at the initial state
: <math> h_{2a}</math> is the [[enthalpy]] at the final state for the actual process
: <math> h_{2s}</math> is the [[enthalpy]] at the final state for the isentropic process

===Minimizing work required by a compressor===

====Comparing reversible to irreversible compressors====

Comparison of the differential form of the energy balance for each device.

Let <math> q </math> be heat, <math> w </math> be work, <math> ke </math> be kinetic energy, and <math> pe </math> be potential energy.

Actual Compressor:<br />
: <math>  \delta q_{act} - \delta w_{actelta q_{act}}{T} \geq 0</math>
<br />Furthermore, <math> ds \geq \frac{\delta q_{act}}{T} </math> and T is [absolute temperature] (<math> T \geq 0 </math>) which produces:<br /><math>   \delta w_{rev} \geq \delta w_{act} </math>

or<br /><math>   w_{rev} \geq w_{act} </math>

Therefore, work-consuming devices such as pumps and compressors (work is negative) require less work when they operate reversibly.<ref name="Cengel, Yunus A. 2012"/>

====Effect of cooling during the compression process====
[[File: Insetropic,polytropic,isothermal.jpg|thumb|P-v (Specific volume vs. Pressure) diagram comparing isentropic, polytropic, and isothermal processes between the same pressure limits.]]

[[isentropic]] process: involves no cooling,<br />
[[polytropic]] process: involves some cooling<br />
[[isothermal]] process: involves maximum cooling

By making the following assumptions the required work for the compressor to compress a gas from <math>P_1 </math> to <math> P_2</math> is the following for each process:
<br />













: <math>P_1 </math> and <math> P_2</math>

: Flow processes VdP
: All processes are internally reversible
: The gas behaves like an [[ideal gas]] with constant [[specific heats]]

Isentropic (<math> Pv^k = constant </math>, where <math>k = C_p/C_v</math>):
<br />
: <math> W_{comp,in}= \frac{kR(T_2-T_1)}{k-1}=\frac{kRT_1}{k-1} \left [  \left ( \frac{P_2}{P_1} \right ) ^{(k-1)/k} -1 \right ] </math>

Polytropic (<math> Pv^n = constant </math>):
<br />
: <math> W_{comp,in}= \frac{nR(T_2-T_1)}{n-1}=\frac{nRT_1}{n-1} \left [  \left ( \frac{P_2}{P_1} \right ) ^{(n-1)/n} -1 \right ] </math>

Isothermal (<math>T = constant</math> or <math>Pv = constant</math>):
<br />
:<math> W_{comp,in}= RT ln \left (  \frac{P_2}{P_1}\right ) </math>

By comparing the three internally reversible processes compressing an ideal gas from <math>P_1 </math> to <math> P_2</math>, the results show that isentropic compression (<math> Pv^k = constant </math>) requires the most work in and the isothermal compression(<math>T = constant</math> or <math>Pv = constant</math>) requires the least amount of work in. For the polytropic process (<math> Pv^n = constant </math>) work decreases as the exponent, n, decreases, by increasing the heat rejection during the compression process. One common way of cooling the gas during compression is to use cooling jackets around the casing of the compressor.<ref name="Cengel, Yunus A. 2012"/>

===Compressors in ideal thermodynamic cycles===
Ideal [[Rankine Cycle]] 1->2 [[Isentropic]] compression in a [[pump]]
<br />
Ideal [[Carnot Cycle]] 4->1 [[Isentropic]] compression
<br />
Ideal [[Otto Cycle]] 1->2 [[Isentropic]] compression
<br />
Ideal [[Diesel Cycle]] 1->2 [[Isentropic]] compression
<br />
Ideal [[Brayton Cycle]] 1->2 [[Isentropic]] compression in a compressor
<br />
Ideal [[Vapor-compression refrigeration | Vapor-compression refrigeration Cycle]] 1->2 [[Isentropic]] compression in a compressor
<br />
NOTE: The isentropic assumptions are only applicable with ideal cycles. Real world cycles have inherent losses due to inefficient compressors and turbines. The real world system are not truly isentropic but are rather idealized as isentropic for calculation purposes.

==Temperature==
{{main|Gas laws}}
Compression of a gas increases its [[temperature]].

For a [[polytropic process|polytropic transformation]] of a gas:

: <math>\begin{cases}
pV^n=\text{constant}=p_1V_1^n=p_2V_2^n \Rightarrow \frac { p_2 }{ p_1 }\ = \left( \frac{ V_1 } { V_2 } \right) ^ n & \\
\frac{p^{\frac{n-1}{n}}}{T}=\text{constant}=\frac{p_1^{\frac{n-1}{n}}}{T_1}=\frac{p_2^{\frac{n-1}{n}}}{T_2} \Rightarrow \left( \frac{ p_2 } { p_1 } \right) ^ \frac{n-1}{n} = \frac{ T_2 } { T_1 } &
\end{cases}</math>

The work done for [[polytropic process|polytropic compression]] (or expansion) of a gas into a closed cylinder.
: <math>W = \int_{V_1}^{V_2} p dV = p_1 V_1^n \int_{V_1}^{V_2} V^{-n} dV = \frac{p_1 V_1^n}{1-n} (V_2^{1-n} - V_1^{1-n}) = \frac{p_1 V_1^n}{1-n} V_1^{1-n} \left( \frac{V_2^{1-n}}{V_1^{1-n}} -1 \right) = \frac{p_1 V_1}{1-n} \left( \frac{V_2^{1-n}}{V_1^{1-n}} -1 \right) = </math>

: <math> = \frac{p_1 V_1}{1-n} \left( \left( \frac{V_1}{V_2} \right)^{n-1} -1 \right) = \frac{p_1 V_1}{1-n} \left( \left( \frac{p_2}{p_1} \right)^{\frac{n-1}{n}} -1 \right) = \frac{p_1 V_1}{1-n} \left( \frac{T_2}{T_1} -1 \right)</math>

so
: <math>W = - \frac{p_1 V_1}{n-1} \left( \left( \frac{p_2}{p_1} \right)^{\frac{n-1}{n}} -1 \right) </math>

in which ''p'' is pressure, ''V'' is volume, ''n'' takes different values for different compression processes (see below), and 1 & 2 refer to initial and final states.

{{anchor|Adiabatic}}
* [[Adiabatic process|Adiabatic]] – This model assumes that no energy (heat) is transferred to or from the gas during the compression, and all supplied work is added to the internal energy of the gas, resulting in increases of temperature and pressure. Theoretical temperature rise is:<ref>''Perry's Chemical Engineer's Handbook'' 8th edition
Perry, Green, page 10-45 section 10-76</ref>
: <math> T_2 = T_1 \left(\frac {p_2}{p_1}\right)^{(\kappa-1)/\kappa} </math>
with ''T''<sub>1</sub> and ''T''<sub>2</sub> in degrees [[Rankine scale|Rankine]] or [[kelvin]]s, ''p''<sub>2</sub> and ''p''<sub>1</sub> being absolute pressures and <math>\kappa = </math> [[Heat capacity ratio|ratio of specific heat]]s (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. Adiabatic compression or expansion more closely model real life when a compressor has good insulation, a large gas volume, or a short time scale (i.e., a high power level). In practice there will always be a certain amount of heat flow out of the compressed gas. Thus, making a perfect adiabatic compressor would require perfect heat insulation of all parts of the machine. For example, even a bicycle tire pump's metal tube becomes hot as you compress the air to fill a tire. The relation between temperature and compression ratio described above means that the value of <math>n</math> for an adiabatic process is <math>\kappa</math> (the ratio of specific heats).

{{anchor|Isothermal}}
* [[Isothermal process|Isothermal]] – This model assumes that the compressed gas remains at a constant temperature throughout the compression or expansion process. In this cycle, internal energy is removed from the system as heat at the same rate that it is added by the mechanical work of compression. Isothermal compression or expansion more closely models real life when the compressor has a large heat exchanging surface, a small gas volume, or a long time scale (i.e., a small power level). Compressors that utilize inter-stage cooling between compression stages come closest to achieving perfect isothermal compression. However, with practical devices perfect isothermal compression is not attainable. For example, unless you have an infinite number of compression stages with corresponding intercoolers, you will never achieve perfect isothermal compression.

For an isothermal process, <math>n</math> is 1, so the value of the work integral for an isothermal process is:
: <math> W = \int_{V_1}^{V_2} p dV = p_1 V_1 \int_{V_1}^{V_2} \frac{1}{V} dV =  p_1 V_1 \ln \frac{V_2}{V_1} = - p_1 V_1 \ln \left( \frac {p_2} {p_1} \right) </math>

When evaluated, the isothermal work is found to be lower than the adiabatic work.

{{anchor|Polytropic}}
* [[Polytropic process|Polytropic]] – This model takes into account both a rise in temperature in the gas as well as some loss of energy (heat) to the compressor's components. This assumes that heat may enter or leave the system, and that input shaft work can appear as both increased pressure (usually useful work) and increased temperature above adiabatic (usually losses due to cycle efficiency). Compression efficiency is then the ratio of temperature rise at theoretical 100 percent (adiabatic) vs. actual (polytropic). Polytropic compression will use a value of <math>n</math> between 0 (a constant-pressure process) and infinity (a constant volume process). For the typical case where an effort is made to cool the gas compressed by an approximately adiabatic process, the value of <math>n</math> will be between 1 and <math>\kappa</math>.

==Staged compression==
In the case of centrifugal compressors, commercial designs currently do not exceed a compression ratio of more than 3.5 to 1 in any one stage (for a typical gas). Since compression raises the temperature, the compressed gas is to be cooled between stages making the compression less adiabatic and more isothermal. The inter-stage coolers (intercoolers) typically result in some partial condensation that is removed in [[vapor–liquid separator]]s.

In the case of small reciprocating compressors, the compressor flywheel may drive a cooling fan that directs ambient air across the [[intercooler]] of a two or more stage compressor.

Because rotary screw compressors can make use of cooling lubricant to reduce the temperature rise from compression, they very often exceed a 9 to 1 compression ratio. 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 × 7 × 7 = 343 [[atmosphere (unit)|atmosphere]]s). ({{convert|343|atm|MPa ksi|sigfig=3|abbr=on|lk=out|disp=or}})

==Drive motors==
There are many options for the motor that powers the compressor:
* Gas [[turbine]]s power the axial and centrifugal flow compressors that are part of [[jet engine]]s.
* [[Steam turbine]]s or [[water turbine]]s are possible for large compressors.
* [[Electric motor]]s are cheap and quiet for static compressors. Small motors suitable for domestic electrical supplies use [[Single-phase electric power|single-phase]] [[alternating current]]. Larger motors can only be used where an industrial electrical [[Three-phase electric power|three phase]] alternating current supply is available.
* [[Diesel engine]]s or [[petrol engine]]s are suitable for portable compressors and support compressors. 
* In automobiles and other types of vehicles (including piston-powered airplanes, boats, trucks, etc.), diesel or gasoline engine's power output can be increased by compressing the intake air, so that more fuel can be burned per cycle. These engines can power compressors using their own crankshaft power (this setup known as a [[supercharger]]), or, use their exhaust gas to drive a turbine connected to the compressor (this setup known as a [[turbocharger]]).

==Lubrication==
Compressors that are driven by an electric motor can be controlled using a [[variable-frequency drive|VFD]] or [[power inverter]], however many hermetic and semi-hermetic compressors can only work in a range of or at fixed speeds, since they may include built-in oil pumps. The built-in oil pump is connected to the same shaft that drives the compressor, and forces oil into the compressor and motor bearings. At low speeds, insufficient quantities of oil reach the bearings, eventually leading to bearing failure, while at high speeds, excessive amounts of oil may be lost from the bearings and compressor and potentially into the discharge line due to splashing. Eventually the oil runs out and the bearings are left unlubricated, leading to failure, and the oil may contaminate the refrigerant, air or other working gas.<ref>{{Cite web|url=https://toshiba-mirai-kagakukan.jp/en/learn/history/ichigoki/1981aircon/index.htm|title=Toshiba Science Museum : World's First Residential Inverter Air Conditioner|website=toshiba-mirai-kagakukan.jp}}</ref>

==Applications==
Gas compressors are used in various applications where either higher pressures or lower volumes of gas are needed:
* In [[pipeline transport]] of purified natural gas from the production site to the consumer, a compressor is driven by a motor fueled by gas bled from the pipeline. Thus, no external power source is necessary.
* In maritime cargo transport and cargo operations by [[gas carrier]]s.
* Petroleum refineries, natural gas processing plants, petrochemical and chemical plants, and similar large industrial plants require compressing for intermediate and end-product gases.
* [[Refrigeration]] and [[air conditioner]] equipment use compressors to move [[heat]] in [[refrigerant]] cycles (see ''[[vapor-compression refrigeration]]'').
* Gas turbine systems compress the intake [[combustion]] air.
* Small-volume purified or manufactured gases require compression to fill high pressure cylinders for [[medical]], [[welding]], and other uses.
* Various industrial, manufacturing, and building processes require [[compressed air]] to power [[pneumatic tools]].
* In the manufacturing and [[blow moulding]] of PET [[plastic bottles]] and containers.
* Some aircraft require compressors to maintain [[cabin pressurization]] at altitude.
* Some types of [[jet engine]]s—such as [[turbojet]]s and [[turbofan]]s—compress the air required for fuel combustion. The jet engine's [[turbine]]s power the combustion air compressor.
* In [[underwater diving]], [[self-contained breathing apparatus]], [[hyperbaric oxygen therapy]], and other life support equipment, compressors provide pressurised [[breathing gas]] either directly or via high pressure gas storage containers, such as [[diving cylinder]]s.<ref name=evil>{{cite journal |title=Compressed breathing air – the potential for evil from within |vauthors=Millar IL, Mouldey PG |year=2008 |volume=38 |issue=2 |pages=145–51 |journal=Diving and Hyperbaric Medicine |publisher=[[South Pacific Underwater Medicine Society]] |url=http://archive.rubicon-foundation.org/7964 |access-date=2009-02-28 |pmid=22692708 |url-status=usurped |archive-url=https://web.archive.org/web/20101225063245/http://archive.rubicon-foundation.org/7964 |archive-date=2010-12-25 }}</ref><ref name=oxyhackers >{{cite book |author=Harlow, V |title=Oxygen Hacker's Companion |publisher=Airspeed Press |year=2002 |isbn=0-9678873-2-1}}</ref> In [[surface supplied diving]], an air compressor is generally used to supply low pressure air (10 to 20 bar) for breathing.
* [[Submarine]]s use compressors to store air for later use in displacing water from buoyancy chambers to adjust buoyancy.
* [[Turbocharger]]s and [[supercharger]]s are compressors that increase [[internal combustion engine]] performance by increasing the mass flow of air inside the cylinder, so the engine can burn more fuel and hence produce more power.
* [[Rail transport|Rail]] and heavy [[road transport]] vehicles use [[compressed air]] to operate [[Air brake (rail)|rail vehicle]] or [[Air brake (road vehicle)|road vehicle]] brakes—and various other systems ([[door]]s, [[windscreen wiper]]s, [[engine]], [[gearbox]] control, etc.).
* Service stations and auto repair shops use compressed air to fill pneumatic [[tire]]s and power pneumatic tools.
* [[Fire piston]]s and [[heat pump]]s exist to heat air or other gasses, and compressing the gas is only a means to that end.
* Rotary lobe compressors are often used to provide air in pneumatic conveying lines for powder or solids. Pressure reached can range from 0.5 to 2 bar g.<ref>{{cite web|url=http://www.powderprocess.net/Equipments%20html/Blowers.html|title=Blowers (Roots)|work=Engineering resources for powder processing industries|publisher=www.powderprocess.net|access-date=15 August 2017|url-status=live|archive-url=https://web.archive.org/web/20170814175023/http://www.powderprocess.net/Equipments%20html/Blowers.html|archive-date=14 August 2017}}</ref>

<gallery>
File:Diving air compressor P8046745.JPG|Diving air compressor in noise reduction cabinet
</gallery>

==See also==
{{colbegin}}
* {{Commonscat-inline|Compressors}}
* {{annotated link|Axial compressor}}
* {{annotated link|Cabin pressurization}}
* {{annotated link|Centrifugal fan}}
* {{annotated link|Compressed air}}
* {{annotated link|Compressed air dryer}}
* {{annotated link|Electrochemical hydrogen compressor}}
* {{annotated link|Fire piston}}
* {{annotated link|Foil bearing}}
* {{annotated link|Hot air engine}}
* {{annotated link|Guided-rotor compressor}}
* {{annotated link|Hydrogen compressor}}
* {{annotated link|Linear compressor}}
* {{annotated link|Liquid-ring pump|Liquid-ring compressor}}
* {{annotated link|Hydride compressor}}
* {{annotated link|Natterer compressor}}
* {{annotated link|Pneumatic cylinder}}
* {{annotated link|Pneumatic tube}}
* {{annotated link|Reciprocating compressor}} (piston compressor)
* {{annotated link|Roots-type supercharger|Roots blower}} (a lobe-type compressor)
* {{annotated link|Slip factor}}
* {{annotated link|Trompe}}
* {{annotated link|Vapor-compression refrigeration}}
* Petko Mukelov - Advanced Analog Sound Compressor Circuit Design - MSc. Diplom Work Technical University Of Sofia, 1984
* {{annotated link|Variable-speed air compressor}}
{{colend}}

==References==
{{Reflist}}

{{HVAC}}

{{Authority control}}

{{DEFAULTSORT:Gas Compressor}}
[[Category:Heating, ventilation, and air conditioning]]
[[Category:Gas compressors| ]]
[[Category:Diving support equipment]]
[[Category:Gas technologies]]
[[Category:Industrial gases]]