<?xml version='1.0' encoding='UTF-8'?><?xml-stylesheet href="http://www.blogger.com/styles/atom.css" type="text/css"?><feed xmlns='http://www.w3.org/2005/Atom' xmlns:openSearch='http://a9.com/-/spec/opensearchrss/1.0/' xmlns:blogger='http://schemas.google.com/blogger/2008' xmlns:georss='http://www.georss.org/georss' xmlns:gd="http://schemas.google.com/g/2005" xmlns:thr='http://purl.org/syndication/thread/1.0'><id>tag:blogger.com,1999:blog-6332634673041173258</id><updated>2024-10-08T12:40:06.105-07:00</updated><title type='text'>CO2 capture</title><subtitle type='html'></subtitle><link rel='http://schemas.google.com/g/2005#feed' type='application/atom+xml' href='http://co2capturemethods.blogspot.com/feeds/posts/default'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/6332634673041173258/posts/default?redirect=false'/><link rel='alternate' type='text/html' href='http://co2capturemethods.blogspot.com/'/><link rel='hub' href='http://pubsubhubbub.appspot.com/'/><author><name>udara sampath</name><uri>http://www.blogger.com/profile/17313623856688943460</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='32' height='24' src='//blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEiIWFzY-w-rwI4piN60McAuXG5JKhsfD4ZvosOejRhXqIcq2KzavP0ruocfayIgbInoVhoUlrEQ773VZrS08PFzKcOwMeOT3dlDC0dVJiOZkga8ByDiPZ69pzFk2uLUqw/s220/DSC01276.JPG'/></author><generator version='7.00' uri='http://www.blogger.com'>Blogger</generator><openSearch:totalResults>1</openSearch:totalResults><openSearch:startIndex>1</openSearch:startIndex><openSearch:itemsPerPage>25</openSearch:itemsPerPage><entry><id>tag:blogger.com,1999:blog-6332634673041173258.post-6245369165633793348</id><published>2011-04-01T15:09:00.001-07:00</published><updated>2011-04-03T12:09:01.770-07:00</updated><title type='text'>CO2-flue gas separation</title><content type='html'>&lt;div class=&quot;MsoNormal&quot; style=&quot;margin-right: .2pt; text-indent: 0cm;&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;/span&gt;&lt;br /&gt;
&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;Coal power plants play a vital role in modern world electricity generation. Electricity generation from the coal-fired power plants is the largest single source CO&lt;sub&gt;2&lt;/sub&gt; emission. &lt;o:p&gt;&lt;/o:p&gt;&lt;/span&gt;&lt;/div&gt;&lt;br /&gt;
&lt;div class=&quot;MsoNormal&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;The total electricity generation according to the source is given in the following figure 1. The coal is used for around 41% electricity generation.&lt;o:p&gt;&lt;/o:p&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;separator&quot; style=&quot;clear: both; text-align: center;&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;a href=&quot;https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEh01hpOVi46iQ-aL6vBnkw2mRfb-B244oHleA4CPye5uUQJ-830oFWm8cpm-i7YSNeXRlnQUwvjTPhedxgsN2fc7OflOseD5w_db1ZTc5MUpWrWVMG4Sm68kMlzv2CPY6MJC7GdxGMlJBU/s1600/Fig-1.jpg&quot; imageanchor=&quot;1&quot; style=&quot;margin-left: 1em; margin-right: 1em;&quot;&gt;&lt;img border=&quot;0&quot; height=&quot;240&quot; src=&quot;https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEh01hpOVi46iQ-aL6vBnkw2mRfb-B244oHleA4CPye5uUQJ-830oFWm8cpm-i7YSNeXRlnQUwvjTPhedxgsN2fc7OflOseD5w_db1ZTc5MUpWrWVMG4Sm68kMlzv2CPY6MJC7GdxGMlJBU/s320/Fig-1.jpg&quot; width=&quot;320&quot; /&gt;&lt;/a&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&amp;nbsp;&amp;nbsp;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoCaption&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;span style=&quot;color: windowtext; font-size: 12pt; font-weight: normal;&quot;&gt;Figure &lt;/span&gt;&lt;span style=&quot;color: windowtext; font-size: 12pt; font-weight: normal;&quot;&gt;1&lt;/span&gt;&lt;span style=&quot;color: windowtext; font-size: 12pt; font-weight: normal;&quot;&gt;:&lt;/span&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;color: windowtext; font-size: 12pt; font-weight: normal;&quot;&gt; Electrical energy generation by different sources&amp;nbsp;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoCaption&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;color: windowtext; font-size: 12pt; font-weight: normal;&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;line-height: 150%; text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;There are six main pollutant gases cause for climate change, CO&lt;sub&gt;2&lt;/sub&gt;, CH&lt;sub&gt;4&lt;/sub&gt;, N&lt;sub&gt;2&lt;/sub&gt;O, SF&lt;sub&gt;6&lt;/sub&gt;, CFC’s and HFC’s. The global warming potential for those gases is given in the table 1. However, CO&lt;sub&gt;2&lt;/sub&gt; has lowest global warming potential. It has highest climate change potential due to the largest emission compare to others. Thus, reduction of CO&lt;sub&gt;2&lt;/sub&gt; is very important for create a better environment.&lt;o:p&gt;&lt;/o:p&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;line-height: 150%; text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;line-height: 150%; text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;br /&gt;
&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;-webkit-border-horizontal-spacing: 2px; -webkit-border-vertical-spacing: 2px;&quot;&gt;&lt;/span&gt;&lt;/span&gt;&lt;br /&gt;
&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: &#39;Times New Roman&#39;;&quot;&gt;&lt;span style=&quot;font-size: 11pt;&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;br /&gt;
&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: &#39;Times New Roman&#39;;&quot;&gt;&lt;span style=&quot;font-size: 11pt;&quot;&gt;Technologies available or being considered for CO&lt;sub&gt;2&lt;/sub&gt;&amp;nbsp;capture are:&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;br /&gt;
&lt;span lang=&quot;EN-US&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;br /&gt;
&lt;br /&gt;
&lt;ul&gt;&lt;li&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: Arial;&quot;&gt;&lt;a href=&quot;http://www.esru.strath.ac.uk/EandE/Web_sites/02-03/carbon_sequestration/Carbon%20Sequestration-423.htm&quot;&gt;Solvent Absorption (Solvent Scrubbing)&lt;/a&gt;&lt;/span&gt;&lt;/span&gt;&lt;/li&gt;
&lt;li&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: Arial;&quot;&gt;&lt;a href=&quot;http://www.esru.strath.ac.uk/EandE/Web_sites/02-03/carbon_sequestration/Carbon%20Sequestration-424.htm&quot;&gt;Physical absorption/adsorption&lt;/a&gt;&lt;/span&gt;&lt;/span&gt;&lt;/li&gt;
&lt;li&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: Arial;&quot;&gt;&lt;a href=&quot;http://www.esru.strath.ac.uk/EandE/Web_sites/02-03/carbon_sequestration/Carbon%20Sequestration-425.htm&quot;&gt;Membrane Systems&lt;/a&gt;&lt;/span&gt;&lt;/span&gt;&lt;/li&gt;
&lt;li&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: Arial;&quot;&gt;&lt;a href=&quot;http://www.esru.strath.ac.uk/EandE/Web_sites/02-03/carbon_sequestration/Carbon%20Sequestration-426.htm&quot;&gt;Cryogenic fractionation&lt;/a&gt;&lt;/span&gt;&lt;/span&gt;&lt;/li&gt;
&lt;li&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span style=&quot;font-family: Arial;&quot;&gt;&lt;a href=&quot;http://www.esru.strath.ac.uk/EandE/Web_sites/02-03/carbon_sequestration/Carbon%20Sequestration-427.htm&quot;&gt;Other options&lt;/a&gt;&lt;/span&gt;&lt;/span&gt;&lt;/li&gt;
&lt;/ul&gt;&lt;span lang=&quot;EN-US&quot;&gt; &lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: x-small;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/span&gt;&lt;br /&gt;
&lt;span lang=&quot;EN-US&quot;&gt;&lt;/span&gt;&lt;br /&gt;
&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;div style=&quot;font-size: medium; margin-bottom: 0px; margin-left: 0px; margin-right: 0px; margin-top: 0px;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;In order to carry on power generation by fossil fuel, CCS technologies are required to reduce the environmental impact by CO&lt;sub&gt;2&lt;/sub&gt;&amp;nbsp;emissions. The post combustion CO&lt;sub&gt;2&lt;/sub&gt;&amp;nbsp;capture via chemical absorption is the most effective and widely used technology in the CO&lt;sub&gt;2&lt;/sub&gt;&amp;nbsp;recovery process.&lt;o:p&gt;&lt;/o:p&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div style=&quot;font-size: medium;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div style=&quot;font-size: medium;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;color: red; font-size: large;&quot;&gt;&lt;b&gt;Research papers&lt;/b&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-size: large;&quot;&gt;&lt;b&gt;&lt;/b&gt;&lt;/span&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: large;&quot;&gt;&lt;b&gt;&lt;/b&gt;&lt;/span&gt;&lt;/span&gt;&lt;br /&gt;
&lt;div align=&quot;center&quot; class=&quot;MsoNormal&quot; style=&quot;display: inline !important; text-align: center;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: large;&quot;&gt;&lt;b&gt;&lt;b&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif; font-size: 14pt;&quot;&gt;1. Comparison of Temperature profiles in CO&lt;sub&gt;2&lt;/sub&gt; removal process with Aspen Plus and MATLAB&amp;nbsp;&lt;/span&gt;&lt;/b&gt;&lt;/b&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;/div&gt;&lt;div&gt;&lt;div align=&quot;center&quot; class=&quot;MsoNormal&quot; style=&quot;display: inline !important; text-align: center;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div align=&quot;center&quot; class=&quot;MsoNormal&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif; font-size: 14pt; font-weight: bold; text-align: center;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;color: blue;&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;Udara S.P.R. Arachchige, &lt;/span&gt;&lt;span lang=&quot;NO-NYN&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;Sanoja A. Jayarathna&lt;/span&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;, Morten C. Melaaen&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div align=&quot;center&quot; class=&quot;MsoNormal&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif; font-weight: bold; text-align: center;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-family: &#39;Times New Roman&#39;; font-weight: normal;&quot;&gt;&lt;b&gt;&lt;/b&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;display: inline !important; text-align: center;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;b&gt;&lt;b&gt;&lt;i&gt;(Published in florida, USA-2011 june)&lt;/i&gt;&lt;/b&gt;&lt;/b&gt;&lt;/span&gt;&lt;/div&gt;&lt;br /&gt;
&lt;div align=&quot;center&quot; class=&quot;MsoNormal&quot; style=&quot;text-align: center;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;&lt;b&gt;&lt;i&gt;&lt;br /&gt;
&lt;/i&gt;&lt;/b&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;&lt;b&gt;&lt;i&gt;Abstract&lt;/i&gt;&lt;/b&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-size: large;&quot;&gt;Carbon dioxide (CO&lt;sub&gt;2&lt;/sub&gt;) has the highest climate change potential due to the largest emission compared to the other sources. Thus, reduction of CO&lt;sub&gt;2&lt;/sub&gt; is very important for creating a better environment. Out of several cleaning methods, post combustion CO&lt;sub&gt;2&lt;/sub&gt; removal by chemical absorption technology is the closest to commercialization. This paper presents a simulation study of the chemical absorption process with the MEA system as the solvent. Data found in literature (Texas case 32 and case 47) are compared with the simulation results. Two models are developed and implemented in Aspen Plus and MATLAB with the same operating conditions and parameters to achieve the given efficiencies as in the Texas pilot plant study. The rate based Electrolyte NRTL model is used in the Aspen Plus model with 32.5w/w % MEA solution and 0.28 as lean CO&lt;sub&gt;2&lt;/sub&gt; loading. The Kent-Eisenberg model is selected for the development of the MATLAB model, and the same MEA system is used. The Kent-Eisenberg is one of the simplest and reliable methods for CO&lt;sub&gt;2&lt;/sub&gt; removal modeling. The simulation results from the Aspen Plus and MATLAB models with the same operating conditions are compared with the temperature profiles. Both models follow similar patterns for the temperature profiles and those approximately equal with the Texas plant data. However, the Aspen Plus model predictions of the temperature seem to be closer compared to that of the MATLAB model.&amp;nbsp;&lt;/span&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;color: red; font-size: large; font-weight: bold;&quot;&gt;&lt;o:p&gt;&lt;/o:p&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;text-align: justify;&quot;&gt;&lt;/div&gt;&lt;div&gt;&lt;div style=&quot;font-size: medium; font-weight: normal;&quot;&gt;&lt;span lang=&quot;EN-US&quot; style=&quot;font-size: 19px; font-weight: 800;&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;color: black; font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;div align=&quot;center&quot; class=&quot;MsoNormal&quot; style=&quot;display: inline !important; margin-bottom: 0px; margin-left: 0px; margin-right: 0px; margin-top: 0px; text-align: center;&quot;&gt;&lt;div style=&quot;font-size: 19px; font-weight: 800;&quot;&gt;&lt;span class=&quot;Apple-style-span&quot; style=&quot;font-family: &#39;Times New Roman&#39;, serif;&quot;&gt;&lt;br /&gt;
&lt;/span&gt;&lt;/div&gt;&lt;/div&gt;&lt;/div&gt;&lt;/div&gt;&lt;/div&gt;&lt;div class=&quot;MsoNormal&quot; style=&quot;font-size: medium; text-align: justify;&quot;&gt;&lt;div style=&quot;margin-bottom: 0px; margin-left: 0px; margin-right: 0px; margin-top: 0px;&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;span lang=&quot;EN-US&quot;&gt;&lt;/span&gt;&lt;/span&gt;&lt;/div&gt;&lt;/div&gt;&lt;/div&gt;&lt;/div&gt;</content><link rel='replies' type='application/atom+xml' href='http://co2capturemethods.blogspot.com/feeds/6245369165633793348/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://co2capturemethods.blogspot.com/2011/04/co2-flue-gas-separation.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/6332634673041173258/posts/default/6245369165633793348'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/6332634673041173258/posts/default/6245369165633793348'/><link rel='alternate' type='text/html' href='http://co2capturemethods.blogspot.com/2011/04/co2-flue-gas-separation.html' title='CO2-flue gas separation'/><author><name>udara sampath</name><uri>http://www.blogger.com/profile/17313623856688943460</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='32' height='24' src='//blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEiIWFzY-w-rwI4piN60McAuXG5JKhsfD4ZvosOejRhXqIcq2KzavP0ruocfayIgbInoVhoUlrEQ773VZrS08PFzKcOwMeOT3dlDC0dVJiOZkga8ByDiPZ69pzFk2uLUqw/s220/DSC01276.JPG'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEh01hpOVi46iQ-aL6vBnkw2mRfb-B244oHleA4CPye5uUQJ-830oFWm8cpm-i7YSNeXRlnQUwvjTPhedxgsN2fc7OflOseD5w_db1ZTc5MUpWrWVMG4Sm68kMlzv2CPY6MJC7GdxGMlJBU/s72-c/Fig-1.jpg" height="72" width="72"/><thr:total>0</thr:total></entry></feed>