<?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-5804407356051242125</id><updated>2024-10-24T12:10:10.188-07:00</updated><category term="Adsorption"/><category term="Adsorption of gases on solids"/><category term="Applications of adsorption"/><category term="Effect  of pressure"/><category term="Effect of temperature"/><category term="Factors infleunce  adsorption of gases on solids"/><category term="Freundlich&#39;s adsorption isotherm"/><category term="Fuller&#39;s earth"/><category term="Ion-exchange resin"/><category term="Langmuir&#39;s adsorption isotherm"/><category term="Role of activated carbon in air"/><category term="Role of adsorbent in catalytic reactions"/><category term="Surface chemistry"/><category term="Vanderwaal&#39;s forces"/><category term="absorption"/><category term="activated charcoal"/><category term="anion exchanger"/><category term="arsening poisoning"/><category term="cation exchanger"/><category term="chemical adsorption"/><category term="chemisorption"/><category term="chromatographic analysis"/><category term="classification of activated carbon"/><category term="condensation process"/><category term="copolymer"/><category term="critical temperature"/><category term="deanionizer"/><category term="decationizer"/><category term="demineralization process"/><category term="derivation of Freundlich adsorption isotherm"/><category term="derivation of Langmuir isotherm"/><category term="evaporation process"/><category term="factors influencing adsorption of solutes from solutions"/><category term="froth floatation process"/><category term="ion-exchange resins"/><category term="mordants"/><category term="negative adsorption"/><category term="physical adsorption"/><category term="physisorption"/><category term="positive adsorption"/><category term="resins"/><category term="silica and aluminum gels"/><category term="waster water treatment"/><category term="zeolite process"/><title type='text'>surface chemistry</title><subtitle type='html'></subtitle><link rel='http://schemas.google.com/g/2005#feed' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/posts/default'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default?redirect=false'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/'/><link rel='hub' href='http://pubsubhubbub.appspot.com/'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><generator version='7.00' uri='http://www.blogger.com'>Blogger</generator><openSearch:totalResults>9</openSearch:totalResults><openSearch:startIndex>1</openSearch:startIndex><openSearch:itemsPerPage>25</openSearch:itemsPerPage><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-9197018546366235342</id><published>2009-11-13T01:41:00.000-08:00</published><updated>2009-11-22T21:33:44.066-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="absorption"/><category scheme="http://www.blogger.com/atom/ns#" term="Adsorption"/><category scheme="http://www.blogger.com/atom/ns#" term="chemisorption"/><category scheme="http://www.blogger.com/atom/ns#" term="physisorption"/><category scheme="http://www.blogger.com/atom/ns#" term="Surface chemistry"/><title type='text'>SURFACE CHEMISTRY</title><content type='html'>&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;    SURFACE CHEMISTRY&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;DEFINITIONS&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Adsorption&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;        It is a&lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt; surface&lt;/strong&gt;&lt;/span&gt; phenomenon. In this, concentration of any molecular species is greater at the surface than in the bulk. The phenomenon of accumulation of gas or liquid molecules on the surface of a solid or liquid is called adsorption.&lt;br /&gt;       The adsorption of gas on a solid is sometimes called occlusion.&lt;br /&gt;   &lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;strong&gt;Ex :&lt;/strong&gt;&lt;/span&gt; &lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;Adsorption of ammonia (adsorbate) in charcoal (adsorbent)&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;            Adsorption of water vapours (adsorbate) on silice gel (adsorbent)&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;            Adsorption of dye (adsorbate) by charcoal (adsorbent) &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;&lt;br /&gt;&lt;/span&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Absorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;span&gt;         It is a bulk phenomenon. It is a process in which, a substance is not only retained on the surface but uniformly distributed throughout the body of the solid or liquid&lt;/span&gt;&lt;br /&gt;      &lt;span style=&quot;color:#cc6600;&quot;&gt;&lt;strong&gt;Ex :&lt;/strong&gt;&lt;/span&gt; &lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;Absorption of ammonia by water &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;             Absorption of water vapours by only CaCl2 &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;            Absorption of water by sponge &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt; &lt;/span&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Adsorbate&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;      The substance on the surface of the solid is called the &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;adsorbate&lt;/span&gt;&lt;/strong&gt;.&lt;br /&gt;      Ex : Various gases (&lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;NH3, CO2, N2, O2 etc&lt;/strong&gt;&lt;/span&gt;.)&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;Adsorbent&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;      The substance to which the adsorbate is attached is called adsorbent.&lt;br /&gt;    &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt; Ex : Silica gel, charcoal, alumina gel, clay, Pd, Pt, Ni &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Sorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;       The process in which both &lt;strong&gt;&lt;span style=&quot;color:#ff0000;&quot;&gt;adsorption and absorption&lt;/span&gt;&lt;/strong&gt; takes place &lt;strong&gt;&lt;span style=&quot;color:#ff0000;&quot;&gt;simultaneously&lt;/span&gt;&lt;/strong&gt;.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Characteristics of adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;            Adsorption is a physical phenomenon but accompanied by a chemical change.&lt;br /&gt;    It is a spontaneous process&lt;br /&gt;    It is a selective process&lt;br /&gt;    It is always accompanied by evolution of heat&lt;br /&gt;    It is specific&lt;br /&gt;    The rate of adsorption depends on temperature.&lt;br /&gt;    It depends on the nature of adsorbent and adsorbate.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Difference between adsorption and absorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt; &lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Adsorption &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;-  Surface phenomenon&lt;br /&gt;-  Rapid process&lt;br /&gt;-  Equilibrium is attained easily&lt;br /&gt;- Concentration of molecule are more on the surface and less in the bulk&lt;br /&gt;- NH3 adsorbed on charcoal&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Absorption &lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;- Bulk Phenomenon&lt;br /&gt;- Slow process&lt;br /&gt;- Equilibrium is slowly , step by a step&lt;br /&gt;- Distribution is uniform&lt;br /&gt;- NH3 absorbed by water&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Types of adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;Adsorption is classified into two types&lt;br /&gt; &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;1. Physical adsorption (or) vander waals adsorption (or) physisorption.&lt;br /&gt;2. chemical adsorption (or) activated adsorption (or) chemisorption&lt;/strong&gt;. &lt;/span&gt;&lt;br /&gt;&lt;span style=&quot;color:#990000;&quot;&gt;&lt;br /&gt;&lt;/span&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Physical adsorption (or) physisorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;           It is the one in which the adsorbed molecules are held on the surface of the adsorbent by weak physical or Vander waal’s forces of attraction.&lt;br /&gt;           &lt;strong&gt;&lt;span style=&quot;color:#660000;&quot;&gt;Ex. Adsorption of H2 (or) O2 on charcoal&lt;/span&gt;&lt;br /&gt;&lt;/strong&gt;&lt;br /&gt;&lt;span&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Chemical adsorption (or) chemisorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;/span&gt;         It is the one in which the adsorbed molecules are held on the surface of the adsorbent by chemical bonds (&lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;covalent bond (or) ionic bond&lt;/strong&gt;&lt;/span&gt;)&lt;br /&gt;          &lt;span style=&quot;color:#660000;&quot;&gt;&lt;strong&gt;Ex.  Adsorption of H2 on NI. &lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Difference between physisorption and chemisorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Physisorption &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt; - Due to inter molecules vander waal’s forces&lt;br /&gt; - Low heat of adsorption (o-40 K.cal/mol/)&lt;br /&gt; - Easy and fast process&lt;br /&gt;  -Reversible&lt;br /&gt; -Decreases with increase in temperature&lt;br /&gt; -The rate of adsorption increase with increases of pressure and concentration&lt;br /&gt;  -Multi layer adsorption occurs&lt;br /&gt;  -Not specific&lt;br /&gt;  -No surface compound form action takes place.&lt;br /&gt;  -Equilibrium is established rapidly&lt;br /&gt;  -Involves very small activation energy&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Chemisorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt; -Due to story chemical bond formation.&lt;br /&gt;- High heat of adsorption(40 – 400 k.cal/mol)&lt;br /&gt; -Difficult and slow process&lt;br /&gt; -Irreversible&lt;br /&gt; -Increases with increases in temperature.&lt;br /&gt; -The rate of adsorption decreases with increase of pressure and concentration.&lt;br /&gt; -Monolayer adsorption occurs.&lt;br /&gt;- Highly specific&lt;br /&gt; -Surface compound formation takes place.&lt;br /&gt; -Requires time&lt;br /&gt; -Involves appreciable activate energy</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/9197018546366235342/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/surface-chemistry.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/9197018546366235342'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/9197018546366235342'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/surface-chemistry.html' title='SURFACE CHEMISTRY'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-6850202640243426330</id><published>2009-11-13T01:40:00.001-08:00</published><updated>2009-11-22T20:35:37.745-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="Adsorption of gases on solids"/><category scheme="http://www.blogger.com/atom/ns#" term="critical temperature"/><category scheme="http://www.blogger.com/atom/ns#" term="Factors infleunce  adsorption of gases on solids"/><category scheme="http://www.blogger.com/atom/ns#" term="Vanderwaal&#39;s forces"/><title type='text'>ADSORPTION OF GASES ON SOLIDS</title><content type='html'>&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;ADSORPTION OF GASES ON SOLIDS&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;The magnitude of adsorption of gases by solids depends on the following factors.&lt;br /&gt;  1. Nature of the adsorbent&lt;br /&gt;  2. The surface area of the adsorbent&lt;br /&gt;  3. Nature of the gases&lt;br /&gt;  4. Pressure of the gas&lt;br /&gt;  5. Temperature of the gas&lt;br /&gt;  6. Reversible character of the adsorbed gases&lt;br /&gt;  7. Activation of the adsorbent&lt;br /&gt; 8. Enthalpy of adsorption&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt; Factors infleunce adsorption of gases on solids&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt; &lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;1. Nature of the adsorbent&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;         The adsorption depends upon the type of adsorbent used. The excellent adsorbents are highly porous in nature. The larger the pores, the greater is the adsorption.&lt;br /&gt;      &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt; Ex : porous substances are silica gel, aluminia and charcoal&lt;/span&gt;&lt;/strong&gt;.&lt;br /&gt;      The adsorption power of these substances can further be enhanced by a pores called &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;activation.&lt;/strong&gt;&lt;/span&gt; During activation, the adsorbent is heated in steam to about 1500°c. Heating drives out all impurities and leads to a lager free surface for adsorption.&lt;br /&gt;            &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;Ex. Charcoal adsorbs 0.011 gms of CCl4 at 24°C.&lt;br /&gt;                   Activated charcoal adsorbs 1.48 gm of at 24°C. &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;The surface area of adsorbent&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;        The extent of adsorption depends on the surface area.&lt;br /&gt;   1. The greater the surface area, the greater is the adsorption.&lt;br /&gt;  2. Larger pores on the adsorbent, larger is the adsorption.&lt;br /&gt;                         &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;Ex. Charcoal and silica gel&lt;/strong&gt;&lt;/span&gt; ( excellent adsorbents).&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Nature of gases&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;        The amount of gas adsorbed by a solid depends on the nature of the gas. Easily liquefiable gases like &lt;span style=&quot;color:#660000;&quot;&gt;&lt;strong&gt;Hl, NH3, Cl2, SO2&lt;/strong&gt;&lt;/span&gt; etc., are adsorbed more easily then the permanent gases like H2, N2, O2 etc.,&lt;br /&gt;   This is due to the following reasons :&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;i. Critical temperature&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;         The ease of liquifications depends on its critical temperature (i.e, the maximum temperature above which a gas cannot be liquefied). Thus if the critical temperature of the gas is more, it will be liquefied and adsorbed more readily.&lt;br /&gt;        Ex.  Adsorption of various gases on 1g of activated charcoal.&lt;br /&gt;&lt;br /&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;strong&gt;ii. Vander waal’s forces&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;        Easily liquefiable gases possess greater vander waal’s forces than permanent gases, so they are adsorbed more readily.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/6850202640243426330/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/adsorption-of-gases-on-solids.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/6850202640243426330'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/6850202640243426330'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/adsorption-of-gases-on-solids.html' title='ADSORPTION OF GASES ON SOLIDS'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-8640216888777914874</id><published>2009-11-13T01:30:00.000-08:00</published><updated>2009-11-22T20:09:33.723-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="chemical adsorption"/><category scheme="http://www.blogger.com/atom/ns#" term="Effect  of pressure"/><category scheme="http://www.blogger.com/atom/ns#" term="Effect of temperature"/><category scheme="http://www.blogger.com/atom/ns#" term="physical adsorption"/><title type='text'>EFFECT OF TEMPERATURE,PRESSURE</title><content type='html'>&lt;span style=&quot;color:#3333ff;&quot;&gt; &lt;strong&gt;EFFECT OF TEMPERATURE&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Physical adsorpotion&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;       It occurs rapidly at lower temperature and decreases with increase in temperature.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Chemical adsorption&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;        It increases with increase in temperature and then decreases with the increase of temperature, physical adsorption changes to chemical adsorption.&lt;br /&gt;       For ex.  Nitrogen is physically adsorbed on iron at 190°c. But when the temperature is raised to 500°c, it is chemisorbed to from a nitride.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;EFFECT OF PRESSURE&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;      According to Le-chatlier’s principlel adsorption increases with the increase of pressure. Decreases of pressure causes desorption.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Reversible nature&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Physical adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;          It is a reversible process. The gas adsorbed on to a solid can be removed (desorbed) under reverse conditions of temperature and pressure.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Chemical adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;            It is an irreversible process because a strong chemical bond is formed between adsorbent and adsorbate.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;Heat of adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;             It is defined as the energy liberated when 1g mole of gas is adsorbed on the solid surface.&lt;br /&gt;In physical adsorption, gas molecules concentrate on the solid surface. Thus, it is similar to the condensation of a gas to liquid. So, adsorption is an&lt;span style=&quot;color:#660000;&quot;&gt; &lt;/span&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;&lt;strong&gt;exothermic&lt;/strong&gt; &lt;/span&gt;process. The attraction between the gas molecules and solid surface are due to weak vander waal’s forces. Therefore, the heat of adsorption is very small (about &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;5kcal / mol&lt;/strong&gt;&lt;/span&gt;) for physical adsorption.&lt;br /&gt;        In chemical adsorption, the attractive forces are due to the formation for true chemical bonds. Therefore, the heat of adsorption is large (&lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;20 to 100&lt;/span&gt;&lt;/strong&gt; &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;kcal/mol&lt;/strong&gt;&lt;/span&gt;)&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Thickness of adsorbed layer of gas&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;           Langmuir showed that at low pressure, the physically adsorbed gas forms only one thick molecular layer. However, above a certain pressure, multi-molecular thick layer is formed. In Chemistry ion, the adsorbed gas is one-molecule thick since chemical combination takes place with the adsorbent surface directly.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/8640216888777914874/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/effect-of-temperaturepressure.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/8640216888777914874'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/8640216888777914874'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/effect-of-temperaturepressure.html' title='EFFECT OF TEMPERATURE,PRESSURE'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-2638452228772721553</id><published>2009-11-13T01:25:00.001-08:00</published><updated>2009-11-21T02:01:33.055-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="factors influencing adsorption of solutes from solutions"/><category scheme="http://www.blogger.com/atom/ns#" term="negative adsorption"/><category scheme="http://www.blogger.com/atom/ns#" term="positive adsorption"/><title type='text'>FACTORS INFLUENCING FACTORS  ADSORPTION OF SOLUTES FROM SOLUTION</title><content type='html'>&lt;strong&gt; &lt;span style=&quot;color:#3333ff;&quot;&gt;Factors Influencing Adsorption of solutes from solutions &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;/span&gt;&lt;/strong&gt;&lt;span&gt;&lt;strong&gt;The amount of solute adsorbed by a solid from the solution depends on the following factors.&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;1. Effect of temperature&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;           A rise in temperature increases the kinetic energies of solute particles and hence these particles leave the surfaces and thereby lowering the extent of adsorption.&lt;br /&gt;Frendlich adsorption equation is found suitable to explain the effect of concentration. &lt;br /&gt;         If a graph is drawn between log x/m Vs log c, a straight line is obtained for small changes of concentrations.&lt;br /&gt;i) when the solute is adsorbed by an adsorbent it is called positive adsorption.&lt;br /&gt;ii) But of the solvent is taken up by the adsorbent it is called negative adsorption.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;a. Negative adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;             Adsorption of substance from the solution decrease with rise in temperature and decrease in concentration of solution. This type of adsorption is known as negative adsorption.&lt;br /&gt;             &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;Ex.  Adsorption of water&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;    From the dilute solution of KCl, charcoal adsorbs water, thereby the concentration gets increased.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;b. Positive adsorption&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;          Adsorption of substance from solution increases with decreases in temperature and in concentration of solution. This type of adsorption is concentration of solution. This type of adsorption is known as positive adsorption.&lt;br /&gt;        &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;Ex.  Adsorption of salt (KCl)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt; Charcoal adsorbs KCl rather than water thereby salt concentration gets decreased.&lt;br /&gt;&lt;br /&gt; &lt;strong&gt;i) The nature of the solute adsorbed&lt;br /&gt;&lt;/strong&gt;   The extent of adsorption is usually greater when the molecular weight of the solute is high.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;ii) Effect of surface area&lt;/strong&gt;&lt;br /&gt;    If the surface area of the adsorbent is increased, adsorption also increases.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/2638452228772721553/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/factors-influencing-adsorption-of.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/2638452228772721553'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/2638452228772721553'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/factors-influencing-adsorption-of.html' title='FACTORS INFLUENCING FACTORS  ADSORPTION OF SOLUTES FROM SOLUTION'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-8301037614011347081</id><published>2009-11-13T01:04:00.000-08:00</published><updated>2009-11-20T23:47:26.094-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="derivation of Freundlich adsorption isotherm"/><category scheme="http://www.blogger.com/atom/ns#" term="Freundlich&#39;s adsorption isotherm"/><title type='text'>FREUNDLICH’S ADSORPTION ISOTHERM</title><content type='html'>&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;strong&gt;FREUNDLICH’S ADSORPTION ISOTHERM&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;   The relationship between the magnitude of adsorption (&lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;x/m&lt;/span&gt;&lt;/strong&gt;) and &lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;p&lt;/span&gt;&lt;/strong&gt; can be expressed mathematically by an empirical equation known as freundlich adsorption isotherm.&lt;br /&gt;                                           &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;x = KP1/xm&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;where,&lt;br /&gt;             x – amount of gas adsorbed&lt;br /&gt;             m – mob of adsorbent&lt;br /&gt;             P – equilibrium pressure&lt;br /&gt;           t,n – constants (depends on nature of adsorbate, adsorbent and T)&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Derivations of Freundlich&#39;s adsorption isotherm&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;br /&gt;        This equation may be derived from the result observed from the graph .&lt;br /&gt;Thus&lt;br /&gt;     i) At low pressure adsorption increasesX x p&lt;br /&gt;    ii) At high pressure adsorption is almost constant X = constant&lt;br /&gt;    iii) At intermediate (normal) pressure adsorption depends on 0 to 1 power of pressure.&lt;br /&gt;                              &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;X x p 1/n (or) X = KP1/n m&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;where, n = whole number.&lt;br /&gt;The above equation is called freundlich’s adsorption is other.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Testing of Freundlich adsorption isotherm&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;        Taking log on both sides, the equation&lt;br /&gt;          &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;x = KP 1/n&lt;/span&gt;&lt;/strong&gt; becomes&lt;br /&gt;     &lt;span style=&quot;color:#666666;&quot;&gt;&lt;strong&gt; &lt;span style=&quot;color:#990000;&quot;&gt; log x = log k + 1 log p m/ n&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;/span&gt;  on plotting log x/m Vs log p, a straight line is obtained with a scope of 1/n and intercepts log k.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Disadvantages or limitation of Freundlich&#39;s adsorption isotherm&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;br /&gt;1. Freundlich equation is purely empirical and has no theoretical basis.&lt;br /&gt;2. The equation is valid only upto a certain pressure and invalid at higher pressure.&lt;br /&gt;3. The constants K and n are not temperature independent, they vary with temperature.&lt;br /&gt;4. Frendilich’s adsorption isotherm fails when the concentration of the adsorbate is very high.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/8301037614011347081/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/freundlichs-adsorption-isotherm.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/8301037614011347081'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/8301037614011347081'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/freundlichs-adsorption-isotherm.html' title='FREUNDLICH’S ADSORPTION ISOTHERM'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-3128005133782248586</id><published>2009-11-13T00:56:00.000-08:00</published><updated>2009-11-20T23:25:55.328-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="condensation process"/><category scheme="http://www.blogger.com/atom/ns#" term="derivation of Langmuir isotherm"/><category scheme="http://www.blogger.com/atom/ns#" term="evaporation process"/><category scheme="http://www.blogger.com/atom/ns#" term="Langmuir&#39;s adsorption isotherm"/><title type='text'>LANGMUIR’S ADSORPTION ISOTHERM</title><content type='html'>&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt; LANGMUIR’S ADSORPTION ISOTHERM&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;Langmuir derived an equation based on some theoretical considerations. The assumptions of Langmuir’s theory are,&lt;br /&gt;1. Valencies at the surface of the adsorbent are not fully satisfied.&lt;br /&gt;2. The adsorbed gas layer on the solid surface is only one molecule thick.&lt;br /&gt;3. The surface of the solid is homogeneous, so the adsorbed layer is uniform all over the adsorbent.&lt;br /&gt;4. There is no interaction between the adjacent adsorbed molecules.&lt;br /&gt;5. The adsorbed gas molecules do not move around the surface.&lt;br /&gt;6. The process of adsorption is a dynamic process, which consists of two opposite processes.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;Condensation Process &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;   It involves the condensation of the molecules of the gas on the surface of the solid.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Evaporation Process&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;      It involves evaporation of the molecules of the adsorbate from the surface of the adsorbent.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Derivation of Langmuir Isotherm&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;         According to Langmiur’s assumptions, when the gas molecules strike a solid surface, some of the molecules are adsorbed where some are desorbed. Thereby dynamic equilibrium is established between adsorption and desorption.&lt;br /&gt;         Consider an adsorbing surface of area 1 square cm exposed to a gas. Then&lt;br /&gt;&lt;br /&gt;q - Fraction of the surface area covered by gas molecules&lt;br /&gt;1- q - Fraction of the uncovered area (vacant area)&lt;br /&gt;r - Pressure of the gas&lt;br /&gt;&lt;br /&gt;              The rate of adsorption = Ka (1-q)p –      &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;(1)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;              The rate of evaporation desorption of gas molecules = Kd q - &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;(2)&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;Where K1 &amp;amp; K2 are proportionality constant for a given system.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;At equilibrium&lt;/span&gt;&lt;/strong&gt; :&lt;br /&gt;          Rate of adsorption = Rate of desorption&lt;br /&gt;                     Ka(1-q)r    = Kdq&lt;br /&gt;                          Kar        = Kdq+ Karq&lt;br /&gt;                   Kar              = q (Kd+ Kar)&lt;br /&gt;                                     q = Kar/Kd+Kar - &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;(3)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt; Dividing the Eq. (1) by ‘ Kd’ it becomes&lt;br /&gt;                                    q = Ka/Kd) r/ 1+ (Ka/Kd) r&lt;br /&gt;                                   q = K r /  1+ K r&lt;br /&gt;Where, Ka/Kd = b = equilibrium constant, called the adsorption coefficient.&lt;br /&gt;       But the amount of gas adsorbed per gram of the adsorbent (x)/m is proportional to the fraction (q) of the surface covered.&lt;br /&gt; On comparing Eq (2) &amp;amp; (3) it becomes&lt;br /&gt;                 x/k = k’kr /1+kr - &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;(4)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;      where K’ = the new constant.&lt;br /&gt;Equation (4) gives the relation between the amount of gas adsorbed to the pressure of the gas at constant T is known as Langmuir adsorption isotherm.&lt;br /&gt;The above Eq. (4) may be rewritten as&lt;br /&gt;                  1+kr = k’kr / x&lt;br /&gt;               1/k’k + kr / k’k = r/x -  &lt;span style=&quot;color:#990000;&quot;&gt;&lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;(5)&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;&lt;/span&gt;Equation (5) represent a straight line (i.e. &lt;strong&gt;&lt;span style=&quot;color:#660000;&quot;&gt;y = c + mx&lt;/span&gt;&lt;/strong&gt;) If the graph is plotted between r/x Vs r, we should get a straight line with slope k/k’k and the Intercept 1/k’k&lt;br /&gt;This equatin is found valid in all cases.&lt;br /&gt;         &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;          Plot of r/x Vs r&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;Case (1) : At low pressure&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;       If the pressure r is very low k/k’k , the r term is negligible.&lt;br /&gt;        i.e. 1/k’k &gt;&gt; k/k’k r&lt;br /&gt;        Hence Eq. (5) becomes&lt;br /&gt;        1/k’k = r/x (or) x = rk’k - &lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;(6)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;               &lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;x µ r&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;i.e. amount of adsorption per unit weight of adsorbent is directly proportional to the r at low pressure.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;Case (ii) at high pressure&lt;/span&gt;&lt;/strong&gt;.&lt;br /&gt;      If the pressure r is high 1/k’k term is negligilble,&lt;br /&gt;        i.e. k/k’k&lt;br /&gt;        Hence Eq (5) becomes&lt;br /&gt;        k/k’k r = r/x or x = k’ (constant)&lt;br /&gt;        &lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;x = k’p°&lt;/span&gt;&lt;/strong&gt; - &lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;(7)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;i.e. extend of adsorption is independent of pressure of the gas, because the surface becomes completely covered at high pressure.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;Case (ii) At normal pressure&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;  If the pressure r is normal (intermediate) the eq. (7) becomes&lt;br /&gt;    &lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;X = k’pn&lt;/span&gt;&lt;/strong&gt; - &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;(8)&lt;br /&gt;&lt;/strong&gt;&lt;/span&gt;  Where n lies between &lt;strong&gt;0 to 1&lt;br /&gt;&lt;/strong&gt;Equation (8) is called Frendliech’s adsorption isotherm.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Merits &lt;/span&gt;&lt;/strong&gt;–  Langmuir&#39;s adsorption isotherm holds good at low pressure.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Demerits&lt;/span&gt;&lt;/strong&gt; - It fails at high pressure.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/3128005133782248586/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/langmuirs-adsorption-isotherm.html#comment-form' title='1 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/3128005133782248586'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/3128005133782248586'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/langmuirs-adsorption-isotherm.html' title='LANGMUIR’S ADSORPTION ISOTHERM'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>1</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-7984491799772937798</id><published>2009-11-13T00:55:00.000-08:00</published><updated>2009-11-20T23:07:17.867-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="activated charcoal"/><category scheme="http://www.blogger.com/atom/ns#" term="Applications of adsorption"/><category scheme="http://www.blogger.com/atom/ns#" term="arsening poisoning"/><category scheme="http://www.blogger.com/atom/ns#" term="chromatographic analysis"/><category scheme="http://www.blogger.com/atom/ns#" term="froth floatation process"/><category scheme="http://www.blogger.com/atom/ns#" term="Fuller&#39;s earth"/><category scheme="http://www.blogger.com/atom/ns#" term="ion-exchange resins"/><category scheme="http://www.blogger.com/atom/ns#" term="mordants"/><category scheme="http://www.blogger.com/atom/ns#" term="silica and aluminum gels"/><title type='text'>APPLICATIONS OF ADSORPTION</title><content type='html'>&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Applications of Adsorption &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;The process of adsorption finds its application in following areas.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;1. Silica and Alumina Gels&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;These are used as adsorbent for removing moisture and for controlling humidities of room.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;2. Activated charcoal&lt;br /&gt;&lt;/span&gt;&lt;span style=&quot;color:#990000;&quot;&gt;a)&lt;/span&gt;&lt;/strong&gt; It is used in gas masks, which adsorp all underivable (toxic) gases, while purified air passes through its poles.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;b)&lt;/span&gt;&lt;/strong&gt; It is also used for removing colouring matter from the sugar solution and the decoloration in vinegar.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;3. Fuller’s Earth&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;It is used in large quantities for refining petroleum and vegetable oil since it adsorbs unwanted materials.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;4. Mordants&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;These are used in dying industry, which adsorp the colouring matter without attaching to the fabrics.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;5. Froth Flotation process&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;The sulphide ores are freed from silica and other earthy matter by froth – floatation process. (Oil adsorbs sulphilde ores only, but not others).&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;6. Ion – exchange resins&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;Softening of hardwater can be done based on the principle of competing adsorption using ion-exchange resins.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;7. Arsenic poisoning&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;Colloidal ferric hydroxide is administered, which adsorbs arsenic poison and is removed from the 60 day by vomiting.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;8. Chromatographic Analysis&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;Selective adsorption by alumina, magnesia, etc. can be used for separating different pigments and also mixtures of small quantities of organic substances with the help of adsorption chromatography.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;9. Measurement of surface area&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;Surface area of powders and rough surfaces can be measured using adsorption measurements.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/7984491799772937798/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/applications-of-adsorption.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/7984491799772937798'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/7984491799772937798'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/applications-of-adsorption.html' title='APPLICATIONS OF ADSORPTION'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-7972965730603364087</id><published>2009-11-13T00:53:00.000-08:00</published><updated>2009-11-22T21:48:02.889-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="classification of activated carbon"/><category scheme="http://www.blogger.com/atom/ns#" term="Role of activated carbon in air"/><category scheme="http://www.blogger.com/atom/ns#" term="Role of adsorbent in catalytic reactions"/><category scheme="http://www.blogger.com/atom/ns#" term="waster water treatment"/><title type='text'>ROLE OF ADSORBENT IN CATALYTIC REACTIONS</title><content type='html'>&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Role of adsorbent in Catalytic reactions &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;br /&gt;&lt;/span&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Adsorbent in Heterogeneous catalytic reaction&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;         &lt;span&gt;Adsorption plays a major role inmost of the industries. Various manufacturing industrial chemical process are heterogeneously catalyst reactions. The function of catalyst is to increase the rate of the reaction and it does not affect the equilibrium.&lt;br /&gt;&lt;/span&gt;&lt;br /&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;strong&gt;The reaction mechanism includes the following steps.&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;&lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;Step 1 : Adsorption of reactant molecules on the surface of the solid.&lt;br /&gt;Step 2 : Formation of activated complex.&lt;br /&gt;Step 3 : Decomposition of activated complex.&lt;br /&gt;Step 4 : Desorption of products.&lt;br /&gt;&lt;/strong&gt;&lt;/span&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;1. Synthesis of Ammonia (Haber’s Process)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;       For synthesis of ammonia iron is used as catalyst with K2O and Al2O3 as promoters. Promoters are the substances which increase the activity of a catalyst. These promoters change the lattice spacing and increase the peaks and cracks on the catalyst surface.&lt;br /&gt;                                   &lt;span style=&quot;color:#3333ff;&quot;&gt; &lt;strong&gt;Fe + Promoter&lt;/strong&gt;&lt;br /&gt;&lt;/span&gt;                  &lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;N2 + 3H2  -----------&gt;    2NH3&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;2. Gas Masks (Purification)&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;           Gas masks are device, which contain activated charcoal as adsorbent. It has high adsorptive capacity and adsorbs all toxic gases immediately (in &gt;0.1 sec) and reduces the concentration of toxic gases from &lt;span style=&quot;color:#660000;&quot;&gt;&lt;strong&gt;1000 ppm to 1 ppm&lt;/strong&gt;&lt;/span&gt;. The function of gas mask is to purify the air for breathing by adsorbing the poisonous gases and vapours from the atmosphere.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;3. In Oil Industry&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;         For Saturating the unsaturated parts in vegetable oil, nickel catalyst is extensively used.&lt;br /&gt;                       &lt;strong&gt;&lt;span style=&quot;color:#cc0000;&quot;&gt;Vegetable Oil + H2 Ni Vegetable ghee&lt;/span&gt;&lt;/strong&gt;.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Classification of Activated Carbon&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;          Activated carbon is classified into two main classes based on their size and different adsorption capacities.&lt;br /&gt;&lt;br /&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;&lt;strong&gt;1. Granular Activated Carbon &lt;br /&gt;&lt;/strong&gt;&lt;/span&gt;      These types of carbons have a diameter greater than 0.1 mm. It is used for adsorption of gases and vapours.&lt;br /&gt;   Carbon is classified into two main classes based on their size and different adsorption capacities.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;2. Powdered Activated Carbon&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;       These types of carbons have a diameter of less than 200 mesh. It is used for purification of liquids.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Activated of Carbon&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;       During activation, charcoal is heated in stream or air atmosphere to about 1500°C. Heating drives out all the impurities as gases and these by leads to a layer surface for adsorption.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;a. Direct Method&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;       In this method, activation is carried out by heating carbon in steam or air at about 850°C. Heating drives out all the impurities sticking on the surface and blocking the capillary poles. This leads to a large surface area of carbon.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3366ff;&quot;&gt;b. Briquetting Method&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;       The powdered carbon is mixed with wood ear and caustic soda compressed into small briquettes and then heated in steam at 800°C.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;c. Chemical Method&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;         The wood is impregnated with a solution of Zinc Chloride or Phosphoric acid and then carbonized.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Role of Activated carbon in waste water treatment&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;       The waste water contains number of compounds which are resistant to bio-degradation and persist in water even after primary and secondary treatments. These impurities are generally carcinogenic and toxic in nature&lt;br /&gt;      These compounds may be eliminated by passing over a bed of granulated activated carbon (GAC). These compounds present in waste water are adsorbed by charcoal and removed from water.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;a. Treatment of waste water&lt;br /&gt;&lt;/span&gt;&lt;span style=&quot;color:#990000;&quot;&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;1. Using a trickling filter method&lt;/span&gt;&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;           The small quantities of dissolved organic hazardous waste can be removed by this method. The filter consists of a number rectangular or circular vessels. These vessels are packed with &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;granular activated carbon (GAC).&lt;/strong&gt;&lt;/span&gt; GAC has an enormous surface area (about &lt;span style=&quot;color:#990000;&quot;&gt;&lt;strong&gt;1000 m2/g&lt;/strong&gt;&lt;/span&gt;) and is commonly used as adsorbent.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#990000;&quot;&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Process &lt;/span&gt;&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;          The contaminated water is allowed to trickle down through the GAC packed in a series of vessels. As the trickled waste water starts percolating down wards through the granular activated carbon the hazardous organics in polluted water are adsorbed on the porous GAC matrix. The GAC filter after sometime gets clogged with the adsorbed contaminates and hence must be replaced or regenerated for further use.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Regeneration&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;       When the charcoal becomes saturated, it is heated in vacuum to above 1500°C and the adsorbates are driver off.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Activated carbons used in other industries&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt; 1. Refining of sugar, glucose.&lt;br /&gt; 2. Removal of taste &amp;amp; colour of drinking water.&lt;br /&gt; 3. Removal of metals from waste water&lt;br /&gt; 4. Removal of impurities from pharmaceutical.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;Role of activated carbon in air&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;        Finally powdered activated carbon is an excellent adsorbent for the removal of toxic gaseous pollutants of impure air. It is used to remove impurities like NO2, SO2, CO and CO2 from impure air.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;a. Treatment of polluted air &lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#3333ff;&quot;&gt;          &lt;/span&gt;&lt;/strong&gt;Using charcoal adsorption tube -  In this technique, the polluted air is sucked by the tube and is passed through a glass wool. The pollutants in air are adsorbed on the granular activated charcoal.&lt;br /&gt;        The amount of pollutant adsorbed is proportional to the surface area of the adsorbent and the Physics, Chemical characteristics of the adsorbent. The temperature are pressure are maintained during the process. The GAC filter after sometime gets clogged with the adsorbed contaminates. The adsorbed pollutants can be leached with a suitable solvent such as carbon disulphide and the solution is analysed by gas chromatography.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/7972965730603364087/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/role-of-adsorbent-in-catalytic.html#comment-form' title='1 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/7972965730603364087'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/7972965730603364087'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/role-of-adsorbent-in-catalytic.html' title='ROLE OF ADSORBENT IN CATALYTIC REACTIONS'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>1</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5804407356051242125.post-239675731884133313</id><published>2009-11-12T23:39:00.000-08:00</published><updated>2009-11-22T21:35:21.454-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="anion exchanger"/><category scheme="http://www.blogger.com/atom/ns#" term="cation exchanger"/><category scheme="http://www.blogger.com/atom/ns#" term="copolymer"/><category scheme="http://www.blogger.com/atom/ns#" term="deanionizer"/><category scheme="http://www.blogger.com/atom/ns#" term="decationizer"/><category scheme="http://www.blogger.com/atom/ns#" term="demineralization process"/><category scheme="http://www.blogger.com/atom/ns#" term="Ion-exchange resin"/><category scheme="http://www.blogger.com/atom/ns#" term="resins"/><category scheme="http://www.blogger.com/atom/ns#" term="zeolite process"/><title type='text'>ROLE OF ADSORBENTS IN ION–EXCHANGE ADSORPTION</title><content type='html'>&lt;span style=&quot;color:#cc0000;&quot;&gt;&lt;strong&gt;Role of adsorbents in Ion – exchange adsorption&lt;/strong&gt;&lt;br /&gt;&lt;/span&gt;&lt;br /&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;&lt;strong&gt;Definition&lt;/strong&gt;&lt;br /&gt;&lt;/span&gt;&lt;br /&gt;Ion – exchange adsorption is defined as, “&lt;span style=&quot;color:#3333ff;&quot;&gt;the process of releasing&lt;/span&gt;”, the one kind of ion and adsorbing another same kind of ion by an adsorbent”.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;Classification of ion-exchangers&lt;/span&gt;&lt;br /&gt;&lt;/strong&gt;&lt;br /&gt;1. Cation exchange resin or cation exchanger or Decationizer resin.&lt;br /&gt;2. Anion exchange resin or anion exchanger or Deanionizer resin.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;1. Cation exchanger or Decationizer resin :&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;These resins are insoluble in water. When water containing salts like &lt;span style=&quot;color:#3333ff;&quot;&gt;MgCl2, CaCl2&lt;/span&gt; is passed through the cation exchanger, it exchanges cations with other cations present in the hardwater. The resins are made from styrene divi.,benzene,copolymer containing, acidic functional groups like sulphonic(-SO3H) acid. It is represented as &lt;span style=&quot;color:#3333ff;&quot;&gt;RH+&lt;/span&gt;.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;Definition :&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;It is defined as cross – linked polymer containing sulphonic group as integral part of resin and an equivalent amount of &lt;span style=&quot;color:#3333ff;&quot;&gt;H+&lt;/span&gt; ions.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;Process :&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;br /&gt;When the solution, containing certain &lt;span style=&quot;color:#3333ff;&quot;&gt;Ca2+, Mg+&lt;/span&gt; is allowed to pass through it H+ ions are exchanged for cations present in solution.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#993399;&quot;&gt;2RH+ + Ca2+ --&gt; R2 Ca2+ + 2H+&lt;br /&gt;2RH+ + Mg2+ --&gt; 2RMg2+ + 2H+&lt;/span&gt;&lt;br /&gt;&lt;/strong&gt;This process consists of desorption of &lt;span style=&quot;color:#3333ff;&quot;&gt;H+&lt;/span&gt; ions and adsorption of &lt;span style=&quot;color:#3333ff;&quot;&gt;Ca2+, Mg2+&lt;/span&gt; ions by the resin.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc66cc;&quot;&gt;2. Anion exchanger or Deanionizer resin&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;When water is passed through anion exchange column, the resin is capable of exchanging their anions with other anions. The resin consists of quaternary ammonia hydroxide groups &lt;span style=&quot;color:#3333ff;&quot;&gt;(-NR3OH)&lt;/span&gt; or amino group etc., on the benzene rings of styrene – divinyl benzene copolymer. This may be represented as &lt;span style=&quot;color:#3366ff;&quot;&gt;R’OH&lt;/span&gt;_.&lt;br /&gt;&lt;br /&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;&lt;strong&gt;Definition :&lt;/strong&gt;&lt;br /&gt;&lt;/span&gt;&lt;br /&gt;Anion exchange is defined as “Cross-linked polymer containing amino group as integral part of resin and an equivalent amount of &lt;span style=&quot;color:#3366ff;&quot;&gt;OH_&lt;/span&gt; ions.&lt;br /&gt;&lt;br /&gt;&lt;span style=&quot;color:#cc33cc;&quot;&gt;&lt;strong&gt;Process :&lt;/strong&gt;&lt;br /&gt;&lt;/span&gt;&lt;br /&gt;When the solution of another anion is allowed to pass through it, &lt;span style=&quot;color:#000099;&quot;&gt;OH_&lt;/span&gt; ions are exchanged by anion present in the solution.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#993399;&quot;&gt;R+ OH_ + Cl_ --&gt; R+Cl_ + OH_&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;It also involves desorption of OH_ ions and adsorption of Cl_ ion by the resin.&lt;br /&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc66cc;&quot;&gt;Regeneration&lt;/span&gt;&lt;br /&gt;&lt;/strong&gt;&lt;br /&gt;When the cation exchange resin is exhausted it can be regenerated by passing a solution of dil. HCl.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#993399;&quot;&gt;R2 Ca 2+ 2H+ --&gt; 2RH+ + Ca2+&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;When the anion exchange column is exhausted it can be regenerated by passing a solution of dil.NaOH.&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#993399;&quot;&gt;R+ Cl_ + OH_ --&gt; R+ OH_ + Cl_&lt;br /&gt;&lt;/span&gt;&lt;/strong&gt;&lt;br /&gt;&lt;strong&gt;&lt;span style=&quot;color:#cc66cc;&quot;&gt;Applications of Ion – exchange Adsorption&lt;/span&gt;&lt;br /&gt;&lt;/strong&gt;&lt;br /&gt;a. In this process not only hardness causing salts are removed, but also salts of trace metal from the water. E.g. &lt;span style=&quot;color:#3366ff;&quot;&gt;Zeolite process&lt;/span&gt; and &lt;span style=&quot;color:#3333ff;&quot;&gt;demineralization process&lt;/span&gt; etc.&lt;br /&gt;b. Complex metal ions such as copper and nicked also can be removed from water used in industries.&lt;br /&gt;c. Ion exchange technique can be applied for concentration of uranium in pitchblende ore.</content><link rel='replies' type='application/atom+xml' href='http://surfacechemis.blogspot.com/feeds/239675731884133313/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/role-of-adsorbents-in-ion-exchange.html#comment-form' title='2 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/239675731884133313'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5804407356051242125/posts/default/239675731884133313'/><link rel='alternate' type='text/html' href='http://surfacechemis.blogspot.com/2009/11/role-of-adsorbents-in-ion-exchange.html' title='ROLE OF ADSORBENTS IN ION–EXCHANGE ADSORPTION'/><author><name>lokina</name><uri>http://www.blogger.com/profile/05390755314744626586</uri><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><thr:total>2</thr:total></entry></feed>