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Economizer

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Economizers (US andOxford spelling), oreconomisers (UK), aremechanical devices intended to reduceenergy consumption, or to perform useful function such as preheating afluid. The term economizer is used for other purposes as well.Boiler, power plant, heating,refrigeration, ventilating, and air conditioning (HVAC) may all use economizers. In simple terms, an economizer is aheat exchanger.

Stirling engine

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Robert Stirling's innovative contribution to the design ofhot air engines of 1816 was what he called the 'Economiser'. Later known as the regenerator, it stored heat from the hot portion of theengine as the air passed to the cold side, and released heat to the cooled air as it returned to the hot side. This innovation improved the efficiency of theStirling engine enough to make it commercially successful in particular applications, and has since been a component of every air engine that is called a Stirling engine.

Boilers

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Inboilers, economizers are heat exchange devices that heat fluids, usually water, up to but not normally beyond theboiling point of that fluid. Economizers are so named because they can make use of theenthalpy in fluid streams that are hot, but not hot enough to be used in a boiler, thereby recovering more useful enthalpy and improving the boiler's efficiency. They are a device fitted to a boiler which saves energy by using theexhaust gases from the boiler to preheat the cold water used to fill it (thefeed water).

Steam boilers use large amounts of energy raising feed water to the boiling temperature, converting the water to steam and sometimessuperheating that steam abovesaturation temperature. Heat transfer efficiency is improved when the highest temperatures near thecombustion sources are used for boiling and superheating, while using the residual heat of the cooled combustion gases exhausting from the boiler through an economizer to raise the temperature of feed water entering the steam drum.

An indirect contact or direct contact condensing economizer will recover the residual heat from the combustion products. A series of dampers, an efficient control system, as well as a ventilator, allow all or part of the combustion products to pass through the economizer, depending on the demand for make-up water and/or process water. The temperature of the gases can be lowered from the boiling temperature of the fluid to little more than the incoming feed water temperature while preheating that feed water to the boiling temperature. High pressure boilers typically have larger economizer surfaces than low pressure boilers. Economizer tubes often have projections like fins to increase the heat transfer surface on the combustion gas side.[1] On average over the years,[clarification needed] boilercombustion efficiency has risen from 80% to more than 95%. The efficiency of heat produced is directly linked toboiler efficiency. The percentage of excess air and the temperature of the combustion products are two key variables in evaluating this efficiency.

Thecombustion ofnatural gas needs a certain quantity of air in order to be complete, so the burners need a flow of excess air in order to operate. Combustion produces water steam, and the quantity depends on the amount of natural gas burned. Also, the evaluation of the dew point depends on the excess air. Natural gas has different combustion efficiency curves linked to the temperature of the gases and the excess air. For example, if the gases[clarification needed] are chilled to 38 °C and there is 15% excess air, then the efficiency will be 94%.[citation needed] The condensing economizer can thus recover the sensible and latent heat in the steam condensate contained in the flue gases for the process.The economizer is made of an aluminium and stainless steel alloy.[citation needed] The gases pass through the cylinder, and the water passes through the finned tubes. It condenses about 11% of the water contained in the gases.[citation needed]

History

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One of two original 1940s 'Green's Economisers' inside theKillafaddy Board Mills boiler house on the outskirts ofLaunceston

The first successful economizer design was used to increase the steam-raisingefficiency of the boilers ofstationary steam engines. It was patented by Edward Green in 1845, and since then has been known asGreen's economiser. It consisted of an array of verticalcast iron tubes connected to a tank of water above and below, between which the boiler's exhaust gases passed. This is the reverse arrangement to that usually but not always seen in the fire tubes of a boiler; there the hot gases usually pass through tubes immersed in water, whereas in an economizer the water passes through tubes surrounded by hot gases. While both are heat exchange devices, in aboiler the burning gases heat the water to producesteam to drive anengine, whether piston or turbine, whereas in aneconomizer, some of the heat energy that would otherwise all be lost to the atmosphere is instead used to heat the water and/or air that will go into the boiler, thus saving fuel. The most successful feature of Green's design of economizer was its mechanical scraping apparatus, which was needed to keep the tubes free of deposits ofsoot.

Economizers were eventually fitted to virtually all stationary steam engines in the decades following Green's invention. Some preserved stationary steam engine sites still have their Green's economisers although usually they are not used. One such preserved site is theClaymills Pumping Engines Trust in Staffordshire, England, which is in the process of restoring one set of economisers and the associated steam engine which drove them. Another such example is theBritish Engineerium in Brighton & Hove, where the economiser associated with the boilers for Number 2 Engine is in use, complete with its associated small stationary engine. A third site isColdharbour Mill Working Wool Museum, where the Green's economiser is in working order, complete with the drive shafts from the Pollit and Wigzell steam engine.

Power plants

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Main article:Feedwater heater

Modern-dayboilers, such as those incoal-firedpower stations, are still fitted with economizers which are descendants of Green's original design. In this context they are often referred to asfeedwater heaters and heat the condensate fromturbines before it is pumped to the boilers.

Economizers are commonly used as part of aheat recovery steam generator (HRSG) in acombined cycle power plant. In an HRSG, water passes through an economizer, then aboiler and then asuperheater. The economizer also prevents flooding of the boiler with liquid water that is too cold to be boiled given the flow rates and design of the boiler.

A common application of economizers in steam power plants is to capture thewaste heat fromboiler stack gases (flue gas) and transfer it to the boiler feedwater. This raises the temperature of the boiler feedwater, lowering the needed energy input, in turn reducing the firing rates needed for the rated boiler output. Economizers lower stack temperatures which may cause condensation of acidic combustion gases and serious equipmentcorrosion damage if care is not taken in their design and material selection.

HVAC

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A building'sHVAC (heating, ventilating, and air conditioning) system can make use of anair-side economizer to save energy in buildings by using cool outside air as a means of cooling the indoor space. When the temperature of the outside air is less than the temperature of the recirculated air, conditioning with the outside air is more energy efficient than conditioning with recirculated air. When the outside air is both sufficiently cool and sufficiently dry (depending on the climate) the amount of enthalpy in the air is acceptable and no additional conditioning of it is needed; this portion of the air-side economizer control scheme is calledfree cooling.

Air-side economizers can reduceHVAC energy costs in cold and temperate climates while also potentially improvingindoor air quality, but are most often not appropriate in hot andhumid climates. With the appropriate controls, economizers can be used in climates which experience various weather systems.[2]

When the outside air's dry- and wet-bulb temperatures are low enough, awater-side economizer can use water cooled by a wetcooling tower or a dry cooler (also called a fluid cooler) to cool buildings without operating achiller. They are historically known as thestrainer cycle, but the water-side economizer is not a truethermodynamic cycle. Also, instead of passing the cooling tower water through a strainer and then to the cooling coils, which causesfouling, more often a plate-and-frame heat exchanger is inserted between the cooling tower and chilled water loops.

Good controls, and valves or dampers, as well as maintenance, are needed to ensure proper operation of the air- and water-side economizers.

Refrigeration

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Cooler economizer

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A common form of refrigeration economizer is a "walk-in cooler economizer" or "outside air refrigeration system". In such a system outside air that is cooler than the air inside a refrigerated space is brought into that space and the same amount of warmer inside air is ducted outside. The resulting cooling supplements or replaces the operation of a compressor-based refrigeration system. If the air inside a cooled space is only about 5 °F warmer than the outside air that replaces it (that is, the ∆T>5 °F) this cooling effect is accomplished more efficiently than the same amount of cooling resulting from a compressor based system. If the outside air is not cold enough to overcome the refrigeration load of the space the compressor system will need to also operate, or the temperature inside the space will rise.

Vapor-compression refrigeration

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Another use of the term occurs in industrial refrigeration, specificallyvapor-compression refrigeration. Normally, the economizer concept is applied when a particular design or feature on therefrigeration cycle, allows a reduction either in the amount ofenergy used from the power grid, in the size of the components (basically thegas compressor's nominal capacity) used to produce refrigeration, or both.For example, for a walk-in freezer that is kept at −20 °F (−29 °C), the main refrigeration components would include: anevaporator coil (a dense arrangement of pipes containing refrigerant and thin metal fins used to remove heat from inside the freezer), fans to blow air over the coil and around the box, an air-cooledcondensing unit sited outdoors, andvalves and piping. The condensing unit would include acompressor and a coil and fans to exchange heat with the ambient air.

An economizer display takes advantage of the fact thatrefrigeration systems have increasing efficiencies at increasing pressures and temperatures. Thepower thegas compressor needs is strongly correlated to both the ratio and the difference, between the discharge and the suction pressures (as well as to other features like therefrigerant's heat capacity and the type of compressor). Low temperature systems such as freezers move less fluid in same volumes. That means the compressor's pumping is less efficient on low temperature systems. This phenomenon is notorious when taking in account that the evaporation temperature for a walk-in freezer at −20 °F (−29 °C) may be around −35 °F (−37 °C).Systems with economizers aim to produce part of the refrigeration work on high pressures, condition in whichgas compressors are normally more efficient. Depending on the application, this technology either allows smaller compression capacities to be able to supply enoughpressure and flow for a system that normally would require bigger compressors, increases the capacity of a system that without economizer would produce less refrigeration, or allows the system to produce the same amount of refrigeration using less power.

The economizer concept is linked tosubcooling as thecondensed liquid line temperature is usually higher than that on theevaporator, making it a good place to apply the notion of increasing efficiencies.[3] Recalling the walk-in freezer example, the normaltemperature of theliquid line in that system is around 60 °F (16 °C) or even higher (it varies depending on the condensing temperature). That condition is by far less hostile to produce refrigeration, than the evaporator at −35 °F (−37 °C).

Economizer setups in refrigeration

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Several configurations of therefrigeration cycle incorporate an economizer, and benefit from this idea. The design of these systems requires expertise and extra components. Pressure drop, electronic valve control, and oil drag, must all be considered.

Two Staged System.
Two staged systems may need to double the pressure handlers installed in the cycle. The diagram displays two differentthermal expansion valves (TXV) and two separate stages ofgas compression.

Two staged systems and boosters

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A system is said to be a two staged set-up if twogas compressors work together in serial to produce the compression. A normal booster installation is a two staged system that receives fluid to cool down the discharge of the first compressor, before it is input to the second compressor. The fluid that arrives at the interstage of both compressors comes from theliquid line and is normally controlled byexpansion, pressure and solenoid valves.

Subcooled Booster Setup.
Asubcooled booster has asubcooling heat exchanger (SHX) that providessubcooling for thecondensed liquid line.

A standard two staged cycle of this kind has anexpansion valve that expands and modulates the amount ofrefrigerant incoming at the interstage. As the fluid arriving at the interstage expands, it will tend toevaporate, producing a temperature drop and cooling the second compressor's suction when mixed with the fluid discharged by the first compressor. This kind of set-up may have aheat exchanger between the expansion and the interstage, which may be a secondevaporator to produce an additional refrigeration effect, though not as cool as the main evaporator (for example to produceair conditioning or for keeping fresh products). A two staged system is said to be set-up as a booster withsubcooling, if the refrigerant arriving at the interstage passes through a subcooling heat exchanger that subcools themain liquid line arriving at the main evaporator of the same system.[4]

Economizer With Flash Tank.
Somescrew compressor manufacturers offer them with economizer. This systems can useflash-gas for the economizer input.

Economizer gas compressors

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The need to use twocompressors in a booster set-up tends to increase the cost of a refrigeration system. A two staged system also needs synchronization, pressure control and lubrication. To reduce these costs, specialized equipment has been developed.

Economizer With Subcooling Exchanger.
Asubcooled economizer reduces the amount ofgas compressors in the system.

Economizer screw compressors are built by several manufacturers like Refcomp, Mycom, Bitzer and York. These machines merge both compressors of a two staged system into onescrew compressor with two inputs: the main suction and an interstage side entrance for higher pressure gas.[citation needed] This means there is no need to install two compressors and still benefit from the booster concept.

There are two types of economizer setups for these compressors,flash andsubcooling. The latter works like a two staged booster with subcooling. The flash economizer is different because it doesn't use aheat exchanger to produce the subcooling. Instead, it has a flash chamber or tank, in which flash gas is produced to lower the temperature of theliquid before the expansion. Theflash gas that is produced in this tank leaves the liquid line and goes to the economizer entrance of the screw compressor.[5]

System With Cycle Optimization.
Refrigeration cycle optimizers such as EcoPac's E-Series, keep the original design of the refrigeration cycle without modification.

Subcooling and refrigeration cycle optimizers

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The above systems produce an economizer effect by using compressors, meters, valves andheat exchangers within the refrigeration cycle. In some refrigeration systems the economizer can be an independent refrigeration mechanism. Such is the case ofsubcooling theliquid line by any other means that draws theheat out of the main system. For example, a heat exchanger that preheats cold water needed for another process or human use, may take heat from the liquid line, effectively subcooling it and increasing the system's capacity.[6]

Recently, machines exclusively designed for this purpose have been developed. In Chile, the manufacturer EcoPac Systems developed a cycle optimizer able to stabilize the temperature of the liquid line and allow either an increase in the refrigeration capacity of the system, or a reduction of thepower consumption.[7] Such systems have the advantage of not interfering with the original design of therefrigeration system and are a way to expand a single staged system that does not possess an economizercompressor.[8]

Internal heat exchangers

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Subcooling may also be produced bysuperheating the gas leaving theevaporator and heading to thegas compressor.[9] These systems withdrawheat from theliquid line and heat up the gas compressor's suction line. This is a very common solution to insure that gas reaches the compressor and liquid reaches thevalve. It also allows maximumheat exchanger use as minimizes the portion of the heat exchangers used to change the temperature of the fluid, and maximizes the volume in which the refrigerantchanges its phase (phenomena involving much more heat flow, the base principle of vapor-compression refrigeration).

An internal heat exchanger is simply a heat exchanger that uses the cold gas leaving the evaporator coil to cool the high-pressure liquid that is headed into the beginning of the evaporator coil via an expansion device. The gas is used to chill a chamber that normally has a series of pipes for the liquid running through it. Thesuperheated gas then proceeds on to the compressor. Thesubcooling term refers to cooling the liquid below its boiling point. 10 °F (5.6 °C) of subcooling means it is 10 °F colder than boiling at a given pressure. As it represents a difference of temperatures, the subcooling value is not measured on an absolute temperature scale, only on a relative scale as a temperature difference.

See also

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References

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  1. ^Principles of Naval Engineering.Washington, D.C.:United States Government Publishing Office. 1970. pp. 239 & 240.
  2. ^"Energy Cost and IAQ Performance of Ventilation Systems and Controls Study". US Environmental Protection Agency. 3 July 2014. Archived fromthe original on October 27, 2021.
  3. ^Danfos, The Influence of Subcooling on Refrigeration Control Quality. Page 2.[1]
  4. ^Danfos, The Influence of Subcooling on Refrigeration Control Quality. Page 6.[2]
  5. ^"Product database - SWEP".www.swep.net.
  6. ^"APS Bussinss Service, Refrigeration Efficiency Measures". Archived fromthe original on June 2, 2012.
  7. ^Pesca y Medioambiente Nº45, New Challenges on Refrigeration, Cycle Optimizers.[3]
  8. ^"Noticias de proveedores". April 12, 2003. Archived fromthe original on January 15, 2013.
  9. ^Refrigerant Subcooling and System Efficiency, The influence of refrigerant subcooling on system efficiency.
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