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Performance analysis of cooling tower using desiccant
Cooling towers are one of the biggest heat and mass transfer devices that are in widespread use. In this work, the cooling tower model has been fabricated and silica gel mesh (SGM) column is installed at the inlet of the cooling tower. Experiments have been performed for three different modes namely...
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Published in: | Heat and mass transfer 2020-04, Vol.56 (4), p.1153-1169 |
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creator | Mishra, Bhavna Srivastava, Aalekh Yadav, Laxmikant |
description | Cooling towers are one of the biggest heat and mass transfer devices that are in widespread use. In this work, the cooling tower model has been fabricated and silica gel mesh (SGM) column is installed at the inlet of the cooling tower. Experiments have been performed for three different modes namely with 0, 1 and 2 silica gel mesh with the subcases of varying air velocity and inlet water temperature. Experimental results demonstrated that the addition of a desiccant column (SGM) at inlet improves the range and effectiveness of the cooling tower. At higher inlet temperature (80°
C
and 4.3 m/s air velocity) the range of 2 SGM cooling tower is 2°
C
greater than without SGM cooling tower. This study also analyzes the effect of SGM column on the cooling water flow rate of the condenser of the thermal power plant and it has been found that required mass flow rate of SGM cooling tower is less than the normal cooling tower at any operating conditions. The minimum value of cooling water flow rate (32.05 kg/s) is achieved when inlet water temperature and velocity are 50°
C
and 3 m/s, respectively. Further, the maximum reduction in cooling water flow rate is 18.22% using two SGM column at 4 m/s velocity and 50°
C
inlet temperature. Hence, this modification helps improve the cooling capacity and reduce the water consumption of the cooling tower. |
doi_str_mv | 10.1007/s00231-019-02759-y |
format | article |
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C
and 4.3 m/s air velocity) the range of 2 SGM cooling tower is 2°
C
greater than without SGM cooling tower. This study also analyzes the effect of SGM column on the cooling water flow rate of the condenser of the thermal power plant and it has been found that required mass flow rate of SGM cooling tower is less than the normal cooling tower at any operating conditions. The minimum value of cooling water flow rate (32.05 kg/s) is achieved when inlet water temperature and velocity are 50°
C
and 3 m/s, respectively. Further, the maximum reduction in cooling water flow rate is 18.22% using two SGM column at 4 m/s velocity and 50°
C
inlet temperature. Hence, this modification helps improve the cooling capacity and reduce the water consumption of the cooling tower.</description><identifier>ISSN: 0947-7411</identifier><identifier>EISSN: 1432-1181</identifier><identifier>DOI: 10.1007/s00231-019-02759-y</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Cooling ; Cooling rate ; Cooling towers ; Cooling water ; Desiccants ; Electric power generation ; Engineering ; Engineering Thermodynamics ; Finite element method ; Heat and Mass Transfer ; Heat transfer ; Industrial Chemistry/Chemical Engineering ; Inlet temperature ; Mass flow rate ; Mass transfer ; Original ; Silica gel ; Silicon dioxide ; Thermal power plants ; Thermodynamics ; Velocity ; Water consumption ; Water flow ; Water temperature</subject><ispartof>Heat and mass transfer, 2020-04, Vol.56 (4), p.1153-1169</ispartof><rights>Springer-Verlag GmbH Germany, part of Springer Nature 2019</rights><rights>2019© Springer-Verlag GmbH Germany, part of Springer Nature 2019</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c356t-49804bb598c7cd27b612c7a22bb335005074569446c63d06cc682f655d91aff63</citedby><cites>FETCH-LOGICAL-c356t-49804bb598c7cd27b612c7a22bb335005074569446c63d06cc682f655d91aff63</cites><orcidid>0000-0002-6772-4797</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Mishra, Bhavna</creatorcontrib><creatorcontrib>Srivastava, Aalekh</creatorcontrib><creatorcontrib>Yadav, Laxmikant</creatorcontrib><title>Performance analysis of cooling tower using desiccant</title><title>Heat and mass transfer</title><addtitle>Heat Mass Transfer</addtitle><description>Cooling towers are one of the biggest heat and mass transfer devices that are in widespread use. In this work, the cooling tower model has been fabricated and silica gel mesh (SGM) column is installed at the inlet of the cooling tower. Experiments have been performed for three different modes namely with 0, 1 and 2 silica gel mesh with the subcases of varying air velocity and inlet water temperature. Experimental results demonstrated that the addition of a desiccant column (SGM) at inlet improves the range and effectiveness of the cooling tower. At higher inlet temperature (80°
C
and 4.3 m/s air velocity) the range of 2 SGM cooling tower is 2°
C
greater than without SGM cooling tower. This study also analyzes the effect of SGM column on the cooling water flow rate of the condenser of the thermal power plant and it has been found that required mass flow rate of SGM cooling tower is less than the normal cooling tower at any operating conditions. The minimum value of cooling water flow rate (32.05 kg/s) is achieved when inlet water temperature and velocity are 50°
C
and 3 m/s, respectively. Further, the maximum reduction in cooling water flow rate is 18.22% using two SGM column at 4 m/s velocity and 50°
C
inlet temperature. Hence, this modification helps improve the cooling capacity and reduce the water consumption of the cooling tower.</description><subject>Cooling</subject><subject>Cooling rate</subject><subject>Cooling towers</subject><subject>Cooling water</subject><subject>Desiccants</subject><subject>Electric power generation</subject><subject>Engineering</subject><subject>Engineering Thermodynamics</subject><subject>Finite element method</subject><subject>Heat and Mass Transfer</subject><subject>Heat transfer</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Inlet temperature</subject><subject>Mass flow rate</subject><subject>Mass transfer</subject><subject>Original</subject><subject>Silica gel</subject><subject>Silicon dioxide</subject><subject>Thermal power plants</subject><subject>Thermodynamics</subject><subject>Velocity</subject><subject>Water consumption</subject><subject>Water flow</subject><subject>Water temperature</subject><issn>0947-7411</issn><issn>1432-1181</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LxDAQQIMoWFf_gKeC5-jkuznK4hcs6EHPIU2TpUu3WZMW6b-3awVvnmYO7w3DQ-iawC0BUHcZgDKCgWgMVAmNpxNUEM4oJqQip6gAzRVWnJBzdJHzbsYlp6xA4s2nENPe9s6XtrfdlNtcxlC6GLu235ZD_PKpHPNxb3xunbP9cInOgu2yv_qdK_Tx-PC-fsab16eX9f0GOybkgLmugNe10JVTrqGqloQ6ZSmta8YEgADFhdScSydZA9I5WdEghWg0sSFItkI3y91Dip-jz4PZxTHNX2ZDmapmU8CRogvlUsw5-WAOqd3bNBkC5pjHLHnMnMf85DHTLLFFyjPcb336O_2P9Q1iS2cK</recordid><startdate>20200401</startdate><enddate>20200401</enddate><creator>Mishra, Bhavna</creator><creator>Srivastava, Aalekh</creator><creator>Yadav, Laxmikant</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0002-6772-4797</orcidid></search><sort><creationdate>20200401</creationdate><title>Performance analysis of cooling tower using desiccant</title><author>Mishra, Bhavna ; Srivastava, Aalekh ; Yadav, Laxmikant</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c356t-49804bb598c7cd27b612c7a22bb335005074569446c63d06cc682f655d91aff63</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Cooling</topic><topic>Cooling rate</topic><topic>Cooling towers</topic><topic>Cooling water</topic><topic>Desiccants</topic><topic>Electric power generation</topic><topic>Engineering</topic><topic>Engineering Thermodynamics</topic><topic>Finite element method</topic><topic>Heat and Mass Transfer</topic><topic>Heat transfer</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Inlet temperature</topic><topic>Mass flow rate</topic><topic>Mass transfer</topic><topic>Original</topic><topic>Silica gel</topic><topic>Silicon dioxide</topic><topic>Thermal power plants</topic><topic>Thermodynamics</topic><topic>Velocity</topic><topic>Water consumption</topic><topic>Water flow</topic><topic>Water temperature</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mishra, Bhavna</creatorcontrib><creatorcontrib>Srivastava, Aalekh</creatorcontrib><creatorcontrib>Yadav, Laxmikant</creatorcontrib><collection>CrossRef</collection><jtitle>Heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mishra, Bhavna</au><au>Srivastava, Aalekh</au><au>Yadav, Laxmikant</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Performance analysis of cooling tower using desiccant</atitle><jtitle>Heat and mass transfer</jtitle><stitle>Heat Mass Transfer</stitle><date>2020-04-01</date><risdate>2020</risdate><volume>56</volume><issue>4</issue><spage>1153</spage><epage>1169</epage><pages>1153-1169</pages><issn>0947-7411</issn><eissn>1432-1181</eissn><abstract>Cooling towers are one of the biggest heat and mass transfer devices that are in widespread use. In this work, the cooling tower model has been fabricated and silica gel mesh (SGM) column is installed at the inlet of the cooling tower. Experiments have been performed for three different modes namely with 0, 1 and 2 silica gel mesh with the subcases of varying air velocity and inlet water temperature. Experimental results demonstrated that the addition of a desiccant column (SGM) at inlet improves the range and effectiveness of the cooling tower. At higher inlet temperature (80°
C
and 4.3 m/s air velocity) the range of 2 SGM cooling tower is 2°
C
greater than without SGM cooling tower. This study also analyzes the effect of SGM column on the cooling water flow rate of the condenser of the thermal power plant and it has been found that required mass flow rate of SGM cooling tower is less than the normal cooling tower at any operating conditions. The minimum value of cooling water flow rate (32.05 kg/s) is achieved when inlet water temperature and velocity are 50°
C
and 3 m/s, respectively. Further, the maximum reduction in cooling water flow rate is 18.22% using two SGM column at 4 m/s velocity and 50°
C
inlet temperature. Hence, this modification helps improve the cooling capacity and reduce the water consumption of the cooling tower.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s00231-019-02759-y</doi><tpages>17</tpages><orcidid>https://orcid.org/0000-0002-6772-4797</orcidid></addata></record> |
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subjects | Cooling Cooling rate Cooling towers Cooling water Desiccants Electric power generation Engineering Engineering Thermodynamics Finite element method Heat and Mass Transfer Heat transfer Industrial Chemistry/Chemical Engineering Inlet temperature Mass flow rate Mass transfer Original Silica gel Silicon dioxide Thermal power plants Thermodynamics Velocity Water consumption Water flow Water temperature |
title | Performance analysis of cooling tower using desiccant |
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