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| + | On the first look there is a huge amount of water available around the “Blue Planet Earth”, but 97% of the worldwide [[Sources_of_water|water resources]] are seawater sources and 2% is locked up in form of polar ice caps. As a result of these facts, less than 0.5% of the worldwide water amount can be used as fresh water source (Akili D. Khawajia*, 2008). |
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375073997|1. Introduction. 2]] | + | By the growing worldwide demand associated to the constantly growing world population water will be one of the rarest resources on the earth in the near future. Several projects around the world are showing that the desalination of seawater is one of the possible options to face the expanding [[Water_scarcity|gap between water demand and water supply]]. Seawater is considered as an almost inexhaustible raw material to gain freshwater from. In this paper the most widely used methods of desalination will be mentioned.<br/> |
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375073998|2. Desalination. 3]]
| + | = Desalination = |
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375073999|2.1. Multi stage flash distillation. 4]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375074000|2.2. Multiple effect distillation. 5]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375074001|2.3. Reverse osmosis. 6]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375074002|Bibliography. 7]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375074003|List of Figures. 7]]
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| − | = 1. Introduction = | + | |
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| − | On the first look there is a huge amount of water available around the “Blue Planet Earth”, but 97% of the worldwide water resources are seawater sources and 2% is locked up in form of polar ice caps. As a result of these facts, less than 0.5% of the worldwide water amount can be used as fresh water source (Akili D. Khawajia*, 2008).
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| − | By the growing worldwide demand associated to the constantly growing world population water will be one of the rarest resources on the earth in the near future. Several projects around the world are showing that the desalination of seawater is one of the possible options to face the expanding gap between water demand and water supply. Seawater is considered as an almost inexhaustible raw material to gain freshwater from. In this paper the most widely used methods of desalination will be mentioned.<br/>
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| − | = 2. Desalination =
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| | The basic principle of the desalination is almost the same in every currently used method. As seen in figure 1 the objective of the different desalination processes is to split the sea or brackish water feed with a certain percentage of salinity in two separate flows: The desalinated, ideally as fresh water usable outcome and the highly concentrated brine which could be described as waste product of desalination. | | The basic principle of the desalination is almost the same in every currently used method. As seen in figure 1 the objective of the different desalination processes is to split the sea or brackish water feed with a certain percentage of salinity in two separate flows: The desalinated, ideally as fresh water usable outcome and the highly concentrated brine which could be described as waste product of desalination. |
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| − | | + | [[File:Desalination principle.png|none|668px|Figure 1: Desalination principle|alt=Figure 1: Desalination principle]]<br/>Source: Economic and technical assessment of desalination technologies; Fawiz Banat |
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| − | Figure 1: Desalination principle<br/>Source: Economic and technical assessment of desalination technologies; Fawiz Banat | + | |
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| | The way how this separation of the inflow is obtained in the desalting device is the counting point for the distinction of the desalination methods. The different methods could be concluded in thermal based methods like distillation or freezing, physical based methods like membrane separation and electrical based methods like the electro dialysis. On the basis of the economic efficiency the mostly used methods are the multi stage flash distillation (MSF) method, the multiple effect distillation (MED) and the reverse osmosis (RO) [fc. (Akili D. Khawajia*, 2008)]. These three most common methods will be described briefly hereinafter. | | The way how this separation of the inflow is obtained in the desalting device is the counting point for the distinction of the desalination methods. The different methods could be concluded in thermal based methods like distillation or freezing, physical based methods like membrane separation and electrical based methods like the electro dialysis. On the basis of the economic efficiency the mostly used methods are the multi stage flash distillation (MSF) method, the multiple effect distillation (MED) and the reverse osmosis (RO) [fc. (Akili D. Khawajia*, 2008)]. These three most common methods will be described briefly hereinafter. |
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| + | == Multi stage flash distillation == |
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| − | == 2.1. Multi stage flash distillation == | + | |
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| | The MSF process is based on the evaporation and condensation of heated sea water. As shown in figure 2 the seawater feed is getting heated up in the heating section and is filled in a series arrangement of tanks with certain temperatures and pressure values. The combination of thermal conditioning and pressure in the tanks allows a continuing steam production even with decreasing temperatures due to the decreasing pressure values in the different stage tanks [fc. (Akili D. Khawajia*, 2008); fc. (ETH-Zürich)] Each tank contains a collector for the condensate that is produced through the cooling function of a heat exchanger which is powered by the cold seawater inflow. | | The MSF process is based on the evaporation and condensation of heated sea water. As shown in figure 2 the seawater feed is getting heated up in the heating section and is filled in a series arrangement of tanks with certain temperatures and pressure values. The combination of thermal conditioning and pressure in the tanks allows a continuing steam production even with decreasing temperatures due to the decreasing pressure values in the different stage tanks [fc. (Akili D. Khawajia*, 2008); fc. (ETH-Zürich)] Each tank contains a collector for the condensate that is produced through the cooling function of a heat exchanger which is powered by the cold seawater inflow. |
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| − | | + | [[File:Multi stage flash destillation (MSF).png|none|604px|Figure 2: Multi Stage Flash Destillation|alt=Figure 2: Multi Stage Flash Destillation]]<br/>Source: SW Infographics; edited by Malte Schümmelfeder |
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| − | Figure 2 Multi Stage Flash distillation (MSF)<br/>Source: SW Infographics; edited by Malte Schümmelfeder | + | |
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| | The efficiency of the desalination process can be increased by the number of stages. As a result of the counter current of the module the cold seawater can be heated up step by step in each stage before it reaches the actual heating section. As part of this pre heating the amount of energy that is needed in the heating section can be decreased. That circumstance has a direct effect of the energy cost of the MSF-module. Modern, large MSF-plants have up to 28 stages [fc. (Akili D. Khawajia*, 2008)]. | | The efficiency of the desalination process can be increased by the number of stages. As a result of the counter current of the module the cold seawater can be heated up step by step in each stage before it reaches the actual heating section. As part of this pre heating the amount of energy that is needed in the heating section can be decreased. That circumstance has a direct effect of the energy cost of the MSF-module. Modern, large MSF-plants have up to 28 stages [fc. (Akili D. Khawajia*, 2008)]. |
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| − | | + | == Multiple effect distillation == |
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| − | == 2.2. Multiple effect distillation == | + | |
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| | The multiple effect distillation is quiet similar to the multi stage flash method. As well as the MSF-method the MED-method is based on the separation of fresh water and salinity due to thermal distillation. Also the different, so called effects could be compared with the different stages within the MSF distillation. In contrast to the flash distillation the incoming seawater is not heated up before it is fed to the first stage to evaporate. It is sprayed on the tube surface of an evaporator located in each effect-containment [fc. (Akili D. Khawajia*, 2008)] This first evaporator is powered by an external source like process heat from power plants. The evaporator in the second effect is supplied by the vapour that arose in the first effect (see figure 3). | | The multiple effect distillation is quiet similar to the multi stage flash method. As well as the MSF-method the MED-method is based on the separation of fresh water and salinity due to thermal distillation. Also the different, so called effects could be compared with the different stages within the MSF distillation. In contrast to the flash distillation the incoming seawater is not heated up before it is fed to the first stage to evaporate. It is sprayed on the tube surface of an evaporator located in each effect-containment [fc. (Akili D. Khawajia*, 2008)] This first evaporator is powered by an external source like process heat from power plants. The evaporator in the second effect is supplied by the vapour that arose in the first effect (see figure 3). |
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| − | | + | [[File:Multiple Effect destillation.png|none|604px|Figure 3: Multiple Effet Destillation|alt=Multi stage flash destillation (MSF).png]]<br/> |
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| | Figure 3: Multiple effect distillation<br/>Source: [http://www.sciencedirect.com/science/article/pii/S1364032111003224 R. Saidur] | | Figure 3: Multiple effect distillation<br/>Source: [http://www.sciencedirect.com/science/article/pii/S1364032111003224 R. Saidur] |
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| − | The vapor that is produced in each effect is clear fresh water which will be conducted through the fresh water output once it is cooled down during the evaporation process in the following effect. The salinity of the remaining brine will be increased in each evaporation process until it is discharged as highly concentrated waste brine after the last effect. Just like in the MSF-distillation the efficiency of the MED-method depends on the number of effects that are cascaded. | + | The vapor that is produced in each effect is clear fresh water which will be conducted through the fresh water output once it is cooled down during the evaporation process in the following effect. The salinity of the remaining brine will be increased in each evaporation process until it is discharged as highly concentrated waste brine after the last effect. Just like in the MSF-distillation the efficiency of the MED-method depends on the number of effects that are cascaded. |
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| + | == Reverse osmosis == |
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| − | == 2.3. Reverse osmosis == | + | |
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| | Unlike the previous mentioned desalination processes the reverse osmosis (RO) is not based on thermodynamically effects. The underlying concept of RO is based on the physical separation of the solved salt through a semipermeable due to imposed pressure. To separate the inflow of seawater into a fresh water flow and waste brine flow the osmotic pressure has to be overboard. The osmotic pressure between two fluids which are separated with a membrane depends on the difference of salinity between the two fluids. As a law of nature the two fluids with different concentration of salinity will always try to reach an osmotic equality due to the molecular exchange through the membrane until the salinity is equal. To prevent this phenomenon the imposed pressure has to be higher than the osmotic pressure. The needed pressure usually ranges between 50 and 80 bar for seawater desalination (Akili D. Khawajia*, 2008). If these conditions are ensured the water will be able to pass through the membrane to the permeate side without any salinity. (see figure 4). | | Unlike the previous mentioned desalination processes the reverse osmosis (RO) is not based on thermodynamically effects. The underlying concept of RO is based on the physical separation of the solved salt through a semipermeable due to imposed pressure. To separate the inflow of seawater into a fresh water flow and waste brine flow the osmotic pressure has to be overboard. The osmotic pressure between two fluids which are separated with a membrane depends on the difference of salinity between the two fluids. As a law of nature the two fluids with different concentration of salinity will always try to reach an osmotic equality due to the molecular exchange through the membrane until the salinity is equal. To prevent this phenomenon the imposed pressure has to be higher than the osmotic pressure. The needed pressure usually ranges between 50 and 80 bar for seawater desalination (Akili D. Khawajia*, 2008). If these conditions are ensured the water will be able to pass through the membrane to the permeate side without any salinity. (see figure 4). |
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| − | | + | [[File:Reverse osmosis.png|left|618px|Figure 4: Reverse osmosis|alt=Figure 4: Reverse osmosis]]<br/>Source: Hydrotec (UK) |
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| − | Figure 4: Reverse osmosis<br/>Source: Hydrotec (UK) | + | |
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| | Beside the two thermal based methods for desalination, the quality of the water which is produced with reverse osmosis depends on several influencing factors. Due to the used amount of pressure, the concentration of salinity in the treated seawater and the size of membranes the quality of the freshwater outflow can be affected (SCCG, 2005). | | Beside the two thermal based methods for desalination, the quality of the water which is produced with reverse osmosis depends on several influencing factors. Due to the used amount of pressure, the concentration of salinity in the treated seawater and the size of membranes the quality of the freshwater outflow can be affected (SCCG, 2005). |
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| | = Bibliography = | | = Bibliography = |
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| | Akili D. Khawajia*, I. K. K. J.-M. W., 2008. Advances in seawater desalination technologies. ''Desalination'', Issue 221, pp. 47-69. | | Akili D. Khawajia*, I. K. K. J.-M. W., 2008. Advances in seawater desalination technologies. ''Desalination'', Issue 221, pp. 47-69. |
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| | SCCG, S. C. C. G., 2005. ''Desalination Fact Sheed, ''sydney: s.n. | | SCCG, S. C. C. G., 2005. ''Desalination Fact Sheed, ''sydney: s.n. |
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| − | = List of Figures =
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072495|Figure 1: Desalination principle]] | + | |
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072495|Source: Economic and technical assessment of desalination technologies; Fawiz Banat. 3]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072496|Figure 2 Multi Stage Flash distillation (MSF)]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072496|Source: SW Infographics; edited by Malte Schümmelfeder. 4]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072497|Figure 3: Multiple effect distillation]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072497|Source: R. Saidur. 5]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072498|Figure 4: Reverse osmosis]]
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| − | [[file:///C:/Users/Skinopolus/Desktop/FH/MASTER/IWRM Sem 1 2013_2014/Water P/Paper Desalination/Output/Desalination Malte Schümmelfeder Wiki-Version.docx#_Toc375072498|Source: Hydrotec (UK). 6]]
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On the first look there is a huge amount of water available around the “Blue Planet Earth”, but 97% of the worldwide water resources are seawater sources and 2% is locked up in form of polar ice caps. As a result of these facts, less than 0.5% of the worldwide water amount can be used as fresh water source (Akili D. Khawajia*, 2008).
By the growing worldwide demand associated to the constantly growing world population water will be one of the rarest resources on the earth in the near future. Several projects around the world are showing that the desalination of seawater is one of the possible options to face the expanding gap between water demand and water supply. Seawater is considered as an almost inexhaustible raw material to gain freshwater from. In this paper the most widely used methods of desalination will be mentioned.
The basic principle of the desalination is almost the same in every currently used method. As seen in figure 1 the objective of the different desalination processes is to split the sea or brackish water feed with a certain percentage of salinity in two separate flows: The desalinated, ideally as fresh water usable outcome and the highly concentrated brine which could be described as waste product of desalination.
Source: Economic and technical assessment of desalination technologies; Fawiz Banat
The way how this separation of the inflow is obtained in the desalting device is the counting point for the distinction of the desalination methods. The different methods could be concluded in thermal based methods like distillation or freezing, physical based methods like membrane separation and electrical based methods like the electro dialysis. On the basis of the economic efficiency the mostly used methods are the multi stage flash distillation (MSF) method, the multiple effect distillation (MED) and the reverse osmosis (RO) [fc. (Akili D. Khawajia*, 2008)]. These three most common methods will be described briefly hereinafter.
The MSF process is based on the evaporation and condensation of heated sea water. As shown in figure 2 the seawater feed is getting heated up in the heating section and is filled in a series arrangement of tanks with certain temperatures and pressure values. The combination of thermal conditioning and pressure in the tanks allows a continuing steam production even with decreasing temperatures due to the decreasing pressure values in the different stage tanks [fc. (Akili D. Khawajia*, 2008); fc. (ETH-Zürich)] Each tank contains a collector for the condensate that is produced through the cooling function of a heat exchanger which is powered by the cold seawater inflow.
The efficiency of the desalination process can be increased by the number of stages. As a result of the counter current of the module the cold seawater can be heated up step by step in each stage before it reaches the actual heating section. As part of this pre heating the amount of energy that is needed in the heating section can be decreased. That circumstance has a direct effect of the energy cost of the MSF-module. Modern, large MSF-plants have up to 28 stages [fc. (Akili D. Khawajia*, 2008)].
The multiple effect distillation is quiet similar to the multi stage flash method. As well as the MSF-method the MED-method is based on the separation of fresh water and salinity due to thermal distillation. Also the different, so called effects could be compared with the different stages within the MSF distillation. In contrast to the flash distillation the incoming seawater is not heated up before it is fed to the first stage to evaporate. It is sprayed on the tube surface of an evaporator located in each effect-containment [fc. (Akili D. Khawajia*, 2008)] This first evaporator is powered by an external source like process heat from power plants. The evaporator in the second effect is supplied by the vapour that arose in the first effect (see figure 3).
The vapor that is produced in each effect is clear fresh water which will be conducted through the fresh water output once it is cooled down during the evaporation process in the following effect. The salinity of the remaining brine will be increased in each evaporation process until it is discharged as highly concentrated waste brine after the last effect. Just like in the MSF-distillation the efficiency of the MED-method depends on the number of effects that are cascaded.
Unlike the previous mentioned desalination processes the reverse osmosis (RO) is not based on thermodynamically effects. The underlying concept of RO is based on the physical separation of the solved salt through a semipermeable due to imposed pressure. To separate the inflow of seawater into a fresh water flow and waste brine flow the osmotic pressure has to be overboard. The osmotic pressure between two fluids which are separated with a membrane depends on the difference of salinity between the two fluids. As a law of nature the two fluids with different concentration of salinity will always try to reach an osmotic equality due to the molecular exchange through the membrane until the salinity is equal. To prevent this phenomenon the imposed pressure has to be higher than the osmotic pressure. The needed pressure usually ranges between 50 and 80 bar for seawater desalination (Akili D. Khawajia*, 2008). If these conditions are ensured the water will be able to pass through the membrane to the permeate side without any salinity. (see figure 4).
Beside the two thermal based methods for desalination, the quality of the water which is produced with reverse osmosis depends on several influencing factors. Due to the used amount of pressure, the concentration of salinity in the treated seawater and the size of membranes the quality of the freshwater outflow can be affected (SCCG, 2005).
Akili D. Khawajia*, I. K. K. J.-M. W., 2008. Advances in seawater desalination technologies. Desalination, Issue 221, pp. 47-69.
Banat, F., 2007. Economic and technical assesment of desalination technologies, Geneva: s.n.
ETH Zürich, n.d. Dampfdrucktabelle Wasser, s.l.: s.n.
SCCG, S. C. C. G., 2005. Desalination Fact Sheed, sydney: s.n.
