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{{Short description|Thermodynamic cycle converting thermal energy into mechanical power}}
{{thermodynamics|cTopic=Processes and Cycles}}
{{thermodynamics|cTopic=Processes and Cycles}}
The '''Hygroscopic Cycle''' is a [[thermodynamic cycle]] converting [[thermal energy]] into mechanical [[power (physics)|power]] by the means of a [[steam turbine]].
The '''Hygroscopic cycle''' is a [[thermodynamic cycle]] converting [[thermal energy]] into mechanical [[power (physics)|power]] by the means of a [[steam turbine]].
It is similar to the [[Rankine cycle]] using [[water]] as the motive fluid but with the novelty of introducing salts and their [[Hygroscopy|hygroscopic]] properties for the [[condensation]]. The salts are desorbed in the [[boiler]] or [[steam]] generator, where clean steam is released and superheated in order to be expanded and generate [[Electric power|power]] through the steam turbine. [[Boiler blowdown]] with the concentrated hygroscocpic compounds is used thermally to pre-heat the steam turbine condensate, and as [[reflux]] in the [[Hygroscopic_cycle#Principles|steam-absorber]].
It is similar to the [[Rankine cycle]] using [[water]] as the motive fluid but with the novelty of introducing salts and their [[Hygroscopy|hygroscopic]] properties for the [[condensation]]. The salts are desorbed in the [[boiler]] or [[steam]] generator, where clean steam is released and superheated in order to be expanded and generate [[Electric power|power]] through the steam turbine. [[Boiler blowdown]] with the concentrated hygroscopic compounds is used thermally to pre-heat the steam turbine condensate, and as [[reflux]] in the [[#Principles|steam-absorber]].


Condensation is done in a steam absorber, as opposed to the traditional condenser found in the [[Rankine cycle]]. Here the outlet steam is absorbed by cooled hygroscopic compounds using the same principles as in [[Absorption refrigerator|absorption refrigarators]]. These hygroscopic compounds are cooled by an air-cooler, where the heat of condensation is dissipated by an air-cooler. Because of the thermal recovery of the boiler blowdown, the hygroscopic reaction in the steam condenser, and the use of an air-cooler to dissipate the heat of condensation, the [[Steam_turbine#Thermodynamics_of_steam_turbines|efficiency]] of the cycle is higher, with a higher electrical output,reduces or eliminates the need for cooling water,<ref name="nrel">{{cite web |url=http://www.nrel.gov/csp/troughnet/pdfs/2007/dersch_dry_cooling.pdf|title=Water efficient cooling of solar thermal power plants}}</ref> [http://www.powermag.com/water/Think-Water-When-Designing-CSP-Plants_4600.html reduces the operating costs], and [http://www.sciencedirect.com/science/article/pii/S1755008413700486 the capital cost of the utility power plant].
Condensation is done in a steam absorber, as opposed to the traditional condenser found in the [[Rankine cycle]]. Here the outlet steam is absorbed by cooled hygroscopic compounds using the same principles as in [[absorption refrigerator]]s. These hygroscopic compounds are cooled by an air-cooler, where the heat of condensation is dissipated by an air-cooler. Because of the thermal recovery of the boiler blowdown, the hygroscopic reaction in the steam condenser, and the use of an air-cooler to dissipate the heat of condensation, the [[Steam turbine#Thermodynamics of steam turbines|efficiency]] of the cycle is higher, with a higher electrical output, reduces or eliminates the need for cooling water,<ref name="nrel">{{cite web|url=http://www.nrel.gov/csp/troughnet/pdfs/2007/dersch_dry_cooling.pdf |title=Water efficient cooling of solar thermal power plants |url-status=dead |archiveurl=https://web.archive.org/web/20131021072413/http://www.nrel.gov/csp/troughnet/pdfs/2007/dersch_dry_cooling.pdf |archive-date=2013-10-21 }}</ref> reduces the operating costs,<ref>{{Cite web|url=http://www.powermag.com/water/Think-Water-When-Designing-CSP-Plants_4600.html|title = Think Water when Designing CSP Plants|website=Powermag.com|date = May 2012}}</ref> and the capital cost of the utility power plant.<ref>{{Cite journal|url=http://www.sciencedirect.com/science/article/pii/S1755008413700486|doi = 10.1016/S1755-0084(13)70048-6|title = The Hygroscopic cycle for CSP|year = 2013|last1 = Rubio|first1 = Francisco Javier|journal = Renewable Energy Focus|volume = 14|issue = 3|page = 18}}</ref>


== Principles ==
== Principles ==
The hygroscopic effect of salts is well known and used in [[Absorption refrigerator]]s where heat is used for [[refrigeration]]. In these machines, the refrigerant is absorbed-dissolved into another fluid (a hygroscopic fluid), reducing its [[partial pressure]] in the evaporator and allowing more liquid to evaporate. In the hygroscopic cycle, the gas absorbed-dissolved into the other fluid is the steam coming from the outlet of the steam turbine. As the steam is absorbed-dissolved into the hygroscopic fluid, more steam can condense, and the reduction in vapor pressure is equivalent to a reduction in the condensation pressure at the outlet of the steam turbine. The effect of this is that a [[steam turbine]] with a lower outlet pressure can be used, with a lower [[enthalpy]] level at the outlet of the turbine. This increases the [[Steam turbine#Thermodynamics of steam turbines|efficiency]] of the turbine, and generates a higher electrical output.


In the steam absorber, steam is absorbed with a concentrated hygroscopic fluid. As the steam is absorbed, the concentration of the hygroscopic fluid decreases, or the salt is [[Enthalpy change of solution|diluted]]. Hygroscopic / [[deliquescence|deliquescent]] fluids with a high dilution capacity in water, such as [[LiBr]] usually also show a [[Saturation temperature#Saturation temperature and pressure|high saturation temperature / low saturation pressure]]. In other words, the [[deliquescence|deliquescent]] [[Solubility#Factors affecting solubility|fluid can condense vapor at a higher temperature]]. This means that the temperature of the concentrated hygroscopic fluid entering the absorber can be higher than a non hygroscopic fluid. As a result, the cooling is easier than in a conventional Rankine cycle in the [[Rankine cycle#The four processes in the Rankine cycle|condensation section]] by using an air-cooler to dissipate the [[Enthalpy of vaporization#Enthalpy of condensation|heat of condensation]] in the [[reflux]]ed concentrated hygroscopic fluid mentioned earlier.
The hygroscopic effect of salts is well known and used in [[Absorption refrigerator]]s where heat is used for [[refrigeration]]. In these machines, the refrigerant is absorbed-dissolved into another fluid (a hygroscopic fluid), reducing its [[partial pressure]] in the evaporator and allowing more liquid to evaporate. In the hygroscopic cycle, the gas absorbed-dissolved into the other fluid is the steam coming from the outlet of the steam turbine. As the steam is absorbed-dissolved into the hygroscopic fluid, more steam can condense, and the reduction in vapor pressure is equivalent to a reduction in the condensation pressure at the outlet of the steam turbine. The effect of this is that a [[steam turbine]] with a lower outlet pressure can be used, with a lower [[enthalpy]] level at the outlet of the turbine. This increases the [[Steam_turbine#Thermodynamics_of_steam_turbines|efficiency]] of the turbine, and generates a higher electrical output.


With the appropriate salts, this can ''reduce, or even eliminate the consumption of cooling water in the power plant''.<ref>{{Cite web|url=https://www.ucsusa.org/resources/water-power-plant-cooling|title=Water for Power Plant Cooling &#124; Union of Concerned Scientists|website=Ucsusa.org|access-date=11 March 2022}}</ref> [[Thermal power station|Cooling water circuits]] in power plants consume a high amount of fresh water<ref>{{Cite web|url=http://www.netl.doe.gov/technologies/coalpower/ewr/pubs/2008_Water_Needs_Analysis-Final_10-2-2008.pdf|title = Home|website=Netl.doe.gov}}</ref><ref name="powermag">{{cite web |url=http://www.powermag.com/water/Water-Conservation-Options-for-Power-Generation-Facilities_4906.html|title=Water Conservation Options for Power Generation Facilities|website=Powermag.com|date=September 2012}}</ref> and chemicals, and their alternative, electric air cooled steam condenser<ref>{{Cite web|url=http://www.hudsonproducts.com/products/stacflo/may22_78.pdf|title = Air Cooled Heat Exchangers &#124; Chart Industries|website=Hudsonproducts.com}}</ref> consumes part of the power produced in conventional power plants, reducing the [[Rankine cycle#Equations|Rankine cycle efficiency]].
In the steam absorber, steam is absorbed with a concentrated hygoscopic fluid. As the steam is absorbed, the concentration of the hygroscopic fluid decreases, or the salt is [[Enthalpy change of solution|diluted]]. Hygroscopic / [[deliquescence|deliquescent]] fluids with a high dilution capacity in water, such as [[LiBr]] usually also show a [[Saturation_temperature#Saturation temperature and pressure|high saturation temperature / low saturation pressure]]. In other words, the [[deliquescence|deliquescent]] [[Solubility#Factors_affecting_solubility|fluid can condense vapor at a higher temperature]]. This means that the temperature of the concentrated hygroscopic fluid entering the absorber can be higher than a non hygroscopic fluid. As a result, the cooling is easier than in a conventional Rankine cycle in the [[Rankine_cycle#The four processes in the Rankine cycle|condensation section]] by using an air-cooler to dissipate the [[Enthalpy_of_vaporization#Enthalpy_of_condensation|heat of condensation]] in the [[reflux]]ed concentrated hygroscopic fluid mentioned earlier.


The air-cooler used in the hygroscopic cycle cools a liquid flow with concentrated hygroscopic compound, with an overall [[volumetric heat capacity]] much higher than the steam traditionally condensed in the air cooled condenser mentioned earlier, thus reducing the power needed for ventilation,<ref>{{Cite web |url=http://www.nidecamerica.com/aircooling/fantech.htm |title=Forced Air Cooling and Fan Technology |access-date=2013-06-07 |archive-date=2013-06-03 |archive-url=https://web.archive.org/web/20130603032618/http://www.nidecamerica.com/aircooling/fantech.htm |url-status=dead }}</ref> and needing less [[Heat transfer coefficient|surface area for heat exchange]] and obtaining a lower overall cost of the plant.<ref name="sciencedirect">{{cite journal |title=The Hygroscopic cycle for CSP |journal=Renewable Energy Focus |volume=14 |issue=3 |pages=18 | doi=10.1016/S1755-0084(13)70048-6|year=2013 |last1=Rubio |first1=Francisco Javier }}</ref>
With the appropriate salts, this can ''reduce, or even eliminate the [http://www.ucsusa.org/clean_energy/our-energy-choices/energy-and-water-use/water-energy-electricity-cooling-power-plant.html consumption of cooling water in the power plant]''. [[Thermal power station|Cooling water circuits]] in power plants [http://www.netl.doe.gov/technologies/coalpower/ewr/pubs/2008_Water_Needs_Analysis-Final_10-2-2008.pdf consume a high amount of fresh water]<ref name="powermag">{{cite web |url=http://www.powermag.com/water/Water-Conservation-Options-for-Power-Generation-Facilities_4906.html|title=Water Conservation Options for Power Generation Facilities}}</ref> and chemicals, and their alternative, electric [http://www.hudsonproducts.com/products/stacflo/may22_78.pdf air cooled steam condenser] consumes part of the power produced in conventional power plants, reducing the [[Rankine_cycle#Equations|Rankine cycle efficiciency]].


[[Thermal power station|Cooling water circuits]] are also expensive, require numerous equipment, such as pumps and cooling towers, and expensive water treatment.<ref>{{cite web|url=http://www-mkk.desy.de/workshop/vortraege/wwt%20Cooling%20Water.pdf|title=Cooling Water : Watertreatment and chemical conditioning of open and closed cooling systems|author=Dr. K. Nachstedt|website=Mkk.desy.de|access-date=March 11, 2022}}</ref> Thus by reducing the cooling water needed, the operating costs of the plant will be reduced.
The air-cooler used in the hygroscopic cycle cools a liquid flow with concentrated hygroscopic compound, with an overall [[Volumetric heat capacity|volumetric heat capcaity]] much higher than the steam traditionally condensed in air cooled condenser mentioned earlier, thus reducing the [http://www.nidecamerica.com/aircooling/fantech.htm power needed for ventilation], and needing less [[Heat transfer coefficient|surface area for heat exchange]] and obtaining a lower overall cost of the plant.<ref name="sciencedirect">{{cite web |url=http://www.sciencedirect.com/science/article/pii/S1755008413700486|title=The Hygroscopic cycle for CSP}}</ref>


Depending on the salts chosen, in particular those with a high dilution capacity (i.e. LiBr), saturation temperature of the hygroscopic fluid can be up to 40&nbsp;°C higher than the steam leaving the turbine.
[[Thermal power station|Cooling water circuits]] are also expensive, require numerous equipment, such as pumps and cooling towers, and [http://www-mkk.desy.de/workshop/vortraege/wwt%20Cooling%20Water.pdf expensive water treatment]. Thus by reducing the cooling water needed, the operating costs of the plant will be reduced.


The salts are concentrated in the boiler, as steam is disengaged from liquid water. Given that the concentration of salts increases, the [[boiling point]] temperature of the mixture of salts is [[Solubility#Factors affecting solubility|affected]]. In most salts, this will [[Boiling-point elevation|increase]] the boiling point temperature, and the steam temperature that is disengaged.<ref name="patentscope.wipo">{{Cite web|url=http://patentscope.wipo.int/search/en/WO2010133726|title = Rankine Cycle with Absorption Step Using Hygroscopic Compounds|website=Patentscope.wipo.int}}</ref>
Depending on the salts chosen, in particular those with a high dilution capacity (i.e. LiBr), saturation temperature of the hygroscopic fluid can be up to 40°C higher than the steam leaving the turbine.

The salts are concentrated in the boiler, as steam is disengaged from liquid water. Given that the concentration of salts increases, the [[boiling point]] temperature of the mixture of salts is [[Solubility#Factors_affecting_solubility|affected]]. In most salts, this will [[Boiling-point elevation|increase]] the boiling point temperature, and the steam temperature that is disengaged.<ref name="patentscope.wipo">http://patentscope.wipo.int/search/en/WO2010133726</ref>


== Hygroscopic Fluids ==
== Hygroscopic Fluids ==


[[Hygroscopy|Hygroscopic compounds]] are all those substances that attract water in vapor or liquid from their environment, thus their use as [[desiccant]]. Many of them react chemically with water such as [[hydrates]] or [[Metal_ions_in_aqueous_solution#Alkali_metals|alcaline metals]]. Others trap water as [[Water_of_crystallization#Position_in_the_crystal_structure|water of hydration]] in their crystalline structure, such as [[sodium sulfate]]. For the last two cases, water can be easily desorbed in a reversible way, as opposed to the first case, where water cannot be recovered easily ([[calcination]] may be required).
[[Hygroscopy|Hygroscopic compounds]] are all those substances that attract water in vapour or liquid from their environment, thus their use as [[desiccant]]. Many of them react chemically with water such as [[hydrates]] or [[Metal ions in aqueous solution#Alkali metals|alkaline metals]]. Others trap water as [[Water of crystallization#Position in the crystal structure|water of hydration]] in their crystalline structure, such as [[sodium sulfate]]. For the last two cases, water can be easily desorbed in a reversible way, as opposed to the first case, where water cannot be recovered easily ([[calcination]] may be required).


The selection of hygroscopic salts have to provide the following strict criteria in order to be of interest of use in the hygroscopic cycle:
The selection of hygroscopic salts have to provide the following strict criteria in order to be of interest of use in the hygroscopic cycle:
* Highly hygroscopic compounds, [[deliquescence|deliquescent]] materials
* Highly hygroscopic compounds, [[deliquescence|deliquescent]] materials
* Less volatile than water ([[vapor pressure]] lower than water), with easily reversible desorbtion into water and steam in the boiler
* Less volatile than water ([[vapor pressure]] lower than water), with easily reversible desorption into water and steam in the boiler
* Good solubility in water at low to moderate temperatures
* Good solubility in water at low to moderate temperatures
* Non-reactivity with other salts in the cycle and chemically stable over the range of temperatures and pressures in the hygroscopic cycle
* Non-reactivity with other salts in the cycle and chemically stable over the range of temperatures and pressures in the hygroscopic cycle
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* Thermal and physical properties are not degraded over cycles
* Thermal and physical properties are not degraded over cycles


Some of the most known salts with similar properties are [[Sodium chloride]], [[Calcium chloride]], [[Naoh|Sodium Hydroxyde]], [[sulfuric acid]] and [[Copper(II) sulfate]]
Some of the most known salts with similar properties are [[Calcium chloride]], [[Naoh|Sodium Hydroxyde]], [[sulfuric acid]] and [[Copper(II) sulfate]]


== Refinements of Hygroscopic Cycle ==
== Refinements of Hygroscopic Cycle ==
Other advantages are that most of the optimisations used in actual [[Rankine cycle]] can be achieved in this Cycle, such as [[rankine cycle#Rankine cycle with reheat|reheat]] and [[rankine cycle#Regenerative Rankine cycle|regeneration]].

Other advantages are that most of the optimisations used in actual [[Rankine cycle]] can be achieved in this Cycle, such as [[rankine_cycle#Rankine_cycle_with_reheat|reheat]] and [[rankine_cycle#Regenerative_Rankine_cycle|regeneration]].


== Hygroscopic Cycle Pilot Plant ==
== Hygroscopic Cycle Pilot Plant ==
A hygroscopic cycle demonstration plant has been built, demonstrating the concepts of the cycle, which includes the [[Absorption (chemistry)|absorption]] of vapour in an absorber where [[Hygroscopy|hygroscopic compounds]] are recirculated, obtaining condensations with temperatures higher than the [[Boiling point#Saturation temperature and pressure|saturation temperature]].<ref>{{Cite web|url=https://www.hygroscopiccycle.com/test-plant/|title=Test plant – Hygroscopic Cycle|website=Hygroscopiccycle.com|access-date=11 March 2022}}</ref> The physical and chemical characteristics of the hygroscopic compounds, as well as their impact on the [[Boiler (power generation)|boiler]], and other main equipment of the cycle similar to those found in [[Power station#Biomass|thermoelectric plants]] have also been proven, together with the overall [[thermodynamic efficiency]] of the cycle.


== Hygroscopic Cycle industrial reference ==
A Pilot plant project is being executed with a power capacity of 100&nbsp;kW. It is expected a conservative 1% increase in power output with a 100% reduction of cooling water, at similar [[capital cost]] as a conventional plant.
The hygroscopic cycle has been introduced in a [[biomass]] power plant in the province of [[Córdoba, Spain|Cordoba, Spain]]. This is the first industrial reference of this technology. It has a capacity of 12.5 MW and is part of Oleicola el Tejar.<ref>{{Cite web |url=http://enipedia.tudelft.nl/wiki/Oleicola_El_Tejar_Scl |title=Oleicola el Tejar SCL - Enipedia |access-date=2017-10-15 |archive-date=2017-10-15 |archive-url=https://web.archive.org/web/20171015203217/http://enipedia.tudelft.nl/wiki/Oleicola_El_Tejar_Scl |url-status=usurped }}</ref> The biomass fed is dried olive bones from the olive oil industry surrounding the plant in the [[Campiña Sur (Córdoba)|south of Cordoba]].<ref>{{Cite journal|title=Combustion Analysis of Different Olive Residues|first1=Teresa|last1=Miranda|first2=Alberto|last2=Esteban|first3=Sebastián|last3=Rojas|first4=Irene|last4=Montero|first5=Antonio|last5=Ruiz|date=4 April 2008|journal=International Journal of Molecular Sciences|volume=9|issue=4|pages=512–525|doi=10.3390/ijms9040512|pmid=19325766|pmc=2635694|doi-access=free}}</ref> The plant was being forced to reduce its production due to water restrictions during high temperatures in the region (the plant consumed 1200 m3/day using adiabatic air coolers<ref>{{Cite web|url=https://www.icscoolenergy.com/sales/product/adiabatic-coolers/|title=Adiabatic Coolers the Sensible Choice for Cooling|website=Icscoolenergy|access-date=11 March 2022}}</ref> from 25&nbsp;°C onwards of ambient temperature). The Hygroscopic cycle has allowed the plant to cut the cooling consumption for these air coolers, increase the power output by 1%, and increase the availability all around the year. The plant can now operate at 38&nbsp;°C, and even 45&nbsp;°C ambient temperature. The owner of the plant can now reach all the generation premiums of this plant. This increase also helps the province to reach the [[2015 United Nations Climate Change Conference|COP 21 agreement]].<ref name="Hygroscopic Cycle industrial reference">{{Cite web |url=http://www.anese.es/20996/ |title=ANESE &#124; IMASA desarrolla una importante tecnología para Oleícola el Tejar que es una herramienta de eficiencia energética muy potente |access-date=2017-10-15 |archive-url=https://web.archive.org/web/20170918013927/http://www.anese.es/20996/ |archive-date=2017-09-18 |url-status=dead }}</ref>
All equipment and materials of the Hygroscopic Cycle are commercial and guaranteed by the different manufacturers.


== State of the art ==
== State of the art ==
The Hygroscopic Cycle is a concept that has evolved recently and is at the heart of intensive research on hygroscopic fluids. Recent developments have been the [[Kalina cycle]],<ref name="google">{{Cite web|url=https://patents.google.com/patent/US6820421|title=Kalina Cycle|website=Google.com|access-date=11 March 2022}}</ref> but with the actual configuration, it is expected to have an impact in locations with poor access to water, and a good integration with [[Bottoming cycle|combined cycle]] plants, and any thermoelectric plants ([[Concentrated solar power|CSP]], biomass, coal). Here the residual heat of the boiler and hygroscopic fluid leaving the boiler can be used for heating purposes.

The Hygroscopic Cycle is a concept that has evolved recently and is at the heart of intensive research on hygroscopic fluids. Recent developments have been the [[Kalina cycle]],<ref name="google">{{cite web |url=http://www.google.com/patents?id=PwgQAAAAEBAJ&dq=6820421+-+Low+temperature+geothermal+system public patent|title=Kalina Cycle}}</ref> but with the actual configuration, it is expected to have an impact in locations with poor access to water, and a good integration with [[Bottoming cycle|combined cycle]] plants, and any thermoelectric plants ([[Concentrated solar power|CSP]], biomass, coal). Here the residual heat of the boiler and hygroscopic fluid leaving the boiler can be used for heating purposes.


The current state of development is being led by Francisco Javier Rubio Serrano, where his research team and company, IMASA INGENIERÍA Y PROYECTOS, S.A. are developing other configurations, and researching hygroscopic fluids for each particular application together with their most suitable construction materials.{{Citation needed|date=May 2013}}
The current state of development is being led by Francisco Javier Rubio Serrano, where his research team and company, IMASA INGENIERÍA Y PROYECTOS, S.A. are developing other configurations, and researching hygroscopic fluids for each particular application together with their most suitable construction materials.{{Citation needed|date=May 2013}}


== References ==
== References ==

{{Reflist}}
{{Reflist}}

{{Thermodynamic cycles|state=uncollapsed}}
{{Thermodynamic cycles|state=uncollapsed}}



Latest revision as of 17:05, 9 June 2024

The Hygroscopic cycle is a thermodynamic cycle converting thermal energy into mechanical power by the means of a steam turbine. It is similar to the Rankine cycle using water as the motive fluid but with the novelty of introducing salts and their hygroscopic properties for the condensation. The salts are desorbed in the boiler or steam generator, where clean steam is released and superheated in order to be expanded and generate power through the steam turbine. Boiler blowdown with the concentrated hygroscopic compounds is used thermally to pre-heat the steam turbine condensate, and as reflux in the steam-absorber.

Condensation is done in a steam absorber, as opposed to the traditional condenser found in the Rankine cycle. Here the outlet steam is absorbed by cooled hygroscopic compounds using the same principles as in absorption refrigerators. These hygroscopic compounds are cooled by an air-cooler, where the heat of condensation is dissipated by an air-cooler. Because of the thermal recovery of the boiler blowdown, the hygroscopic reaction in the steam condenser, and the use of an air-cooler to dissipate the heat of condensation, the efficiency of the cycle is higher, with a higher electrical output, reduces or eliminates the need for cooling water,[1] reduces the operating costs,[2] and the capital cost of the utility power plant.[3]

Principles

[edit]

The hygroscopic effect of salts is well known and used in Absorption refrigerators where heat is used for refrigeration. In these machines, the refrigerant is absorbed-dissolved into another fluid (a hygroscopic fluid), reducing its partial pressure in the evaporator and allowing more liquid to evaporate. In the hygroscopic cycle, the gas absorbed-dissolved into the other fluid is the steam coming from the outlet of the steam turbine. As the steam is absorbed-dissolved into the hygroscopic fluid, more steam can condense, and the reduction in vapor pressure is equivalent to a reduction in the condensation pressure at the outlet of the steam turbine. The effect of this is that a steam turbine with a lower outlet pressure can be used, with a lower enthalpy level at the outlet of the turbine. This increases the efficiency of the turbine, and generates a higher electrical output.

In the steam absorber, steam is absorbed with a concentrated hygroscopic fluid. As the steam is absorbed, the concentration of the hygroscopic fluid decreases, or the salt is diluted. Hygroscopic / deliquescent fluids with a high dilution capacity in water, such as LiBr usually also show a high saturation temperature / low saturation pressure. In other words, the deliquescent fluid can condense vapor at a higher temperature. This means that the temperature of the concentrated hygroscopic fluid entering the absorber can be higher than a non hygroscopic fluid. As a result, the cooling is easier than in a conventional Rankine cycle in the condensation section by using an air-cooler to dissipate the heat of condensation in the refluxed concentrated hygroscopic fluid mentioned earlier.

With the appropriate salts, this can reduce, or even eliminate the consumption of cooling water in the power plant.[4] Cooling water circuits in power plants consume a high amount of fresh water[5][6] and chemicals, and their alternative, electric air cooled steam condenser[7] consumes part of the power produced in conventional power plants, reducing the Rankine cycle efficiency.

The air-cooler used in the hygroscopic cycle cools a liquid flow with concentrated hygroscopic compound, with an overall volumetric heat capacity much higher than the steam traditionally condensed in the air cooled condenser mentioned earlier, thus reducing the power needed for ventilation,[8] and needing less surface area for heat exchange and obtaining a lower overall cost of the plant.[9]

Cooling water circuits are also expensive, require numerous equipment, such as pumps and cooling towers, and expensive water treatment.[10] Thus by reducing the cooling water needed, the operating costs of the plant will be reduced.

Depending on the salts chosen, in particular those with a high dilution capacity (i.e. LiBr), saturation temperature of the hygroscopic fluid can be up to 40 °C higher than the steam leaving the turbine.

The salts are concentrated in the boiler, as steam is disengaged from liquid water. Given that the concentration of salts increases, the boiling point temperature of the mixture of salts is affected. In most salts, this will increase the boiling point temperature, and the steam temperature that is disengaged.[11]

Hygroscopic Fluids

[edit]

Hygroscopic compounds are all those substances that attract water in vapour or liquid from their environment, thus their use as desiccant. Many of them react chemically with water such as hydrates or alkaline metals. Others trap water as water of hydration in their crystalline structure, such as sodium sulfate. For the last two cases, water can be easily desorbed in a reversible way, as opposed to the first case, where water cannot be recovered easily (calcination may be required).

The selection of hygroscopic salts have to provide the following strict criteria in order to be of interest of use in the hygroscopic cycle:

  • Highly hygroscopic compounds, deliquescent materials
  • Less volatile than water (vapor pressure lower than water), with easily reversible desorption into water and steam in the boiler
  • Good solubility in water at low to moderate temperatures
  • Non-reactivity with other salts in the cycle and chemically stable over the range of temperatures and pressures in the hygroscopic cycle
  • Are non-toxic and non flammable
  • Thermal and physical properties are not degraded over cycles

Some of the most known salts with similar properties are Calcium chloride, Sodium Hydroxyde, sulfuric acid and Copper(II) sulfate

Refinements of Hygroscopic Cycle

[edit]

Other advantages are that most of the optimisations used in actual Rankine cycle can be achieved in this Cycle, such as reheat and regeneration.

Hygroscopic Cycle Pilot Plant

[edit]

A hygroscopic cycle demonstration plant has been built, demonstrating the concepts of the cycle, which includes the absorption of vapour in an absorber where hygroscopic compounds are recirculated, obtaining condensations with temperatures higher than the saturation temperature.[12] The physical and chemical characteristics of the hygroscopic compounds, as well as their impact on the boiler, and other main equipment of the cycle similar to those found in thermoelectric plants have also been proven, together with the overall thermodynamic efficiency of the cycle.

Hygroscopic Cycle industrial reference

[edit]

The hygroscopic cycle has been introduced in a biomass power plant in the province of Cordoba, Spain. This is the first industrial reference of this technology. It has a capacity of 12.5 MW and is part of Oleicola el Tejar.[13] The biomass fed is dried olive bones from the olive oil industry surrounding the plant in the south of Cordoba.[14] The plant was being forced to reduce its production due to water restrictions during high temperatures in the region (the plant consumed 1200 m3/day using adiabatic air coolers[15] from 25 °C onwards of ambient temperature). The Hygroscopic cycle has allowed the plant to cut the cooling consumption for these air coolers, increase the power output by 1%, and increase the availability all around the year. The plant can now operate at 38 °C, and even 45 °C ambient temperature. The owner of the plant can now reach all the generation premiums of this plant. This increase also helps the province to reach the COP 21 agreement.[16]

State of the art

[edit]

The Hygroscopic Cycle is a concept that has evolved recently and is at the heart of intensive research on hygroscopic fluids. Recent developments have been the Kalina cycle,[17] but with the actual configuration, it is expected to have an impact in locations with poor access to water, and a good integration with combined cycle plants, and any thermoelectric plants (CSP, biomass, coal). Here the residual heat of the boiler and hygroscopic fluid leaving the boiler can be used for heating purposes.

The current state of development is being led by Francisco Javier Rubio Serrano, where his research team and company, IMASA INGENIERÍA Y PROYECTOS, S.A. are developing other configurations, and researching hygroscopic fluids for each particular application together with their most suitable construction materials.[citation needed]

References

[edit]
  1. ^ "Water efficient cooling of solar thermal power plants" (PDF). Archived from the original (PDF) on 2013-10-21.
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