<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">WJM</journal-id><journal-title-group><journal-title>World Journal of Mechanics</journal-title></journal-title-group><issn pub-type="epub">2160-049X</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/wjm.2011.12009</article-id><article-id pub-id-type="publisher-id">WJM-4674</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Engineering</subject><subject> Physics&amp;Mathematics</subject></subj-group></article-categories><title-group><article-title>
 
 
  Radiative Heat Transfer of an Optically Thick Gray Gas in The Presence of Indirect Natural Convection
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>abindra</surname><given-names>Nath Jana</given-names></name><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Swapan</surname><given-names>Kumar Ghosh</given-names></name><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><author-notes><corresp id="cor1">* E-mail:<email>jana261171@yahoo.co.in(ANJ)</email>;<email>g_swapan2002@yahoo.com(SKG)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>19</day><month>04</month><year>2011</year></pub-date><volume>01</volume><issue>02</issue><fpage>64</fpage><lpage>69</lpage><history><date date-type="received"><day>March</day>	<month>7,</month>	<year>2011</year></date><date date-type="rev-recd"><day>March</day>	<month>30,</month>	<year>2011</year>	</date><date date-type="accepted"><day>April</day>	<month>10,</month>	<year>2011</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  We study the effects of thermal radiation of a viscous incompressible fluid occupying a semi-infinite region of space bounded by an infinite horizontal moving hot flat plate in the presence of indirect natural convection by way of an induced pressure gradient. The fluid is a gray, absorbing emitting radiation but a non scattering medium. An exact solution is obtained by employing Laplace transform technique. Since temperature field depends on Reynold number the flow is considered to be non-isothermal case (the temperature of the plate Tw ≠ constant) and for an isothermal case (Tw = constant) the flow is determined by the Reynold number which is equal to 1.
 
</p></abstract><kwd-group><kwd>Thermal Radiation</kwd><kwd> Indirect Natural Convection</kwd><kwd> Reynold Number</kwd><kwd> Stefan-Boltzman Radiation Parameter</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Thermal radiation of an optically thick gray gas is of great importance to the study of high temperature physics and space technology. Mentioning the study of this type of problem with a view to analyse the transient approach of a radiative heat-transfer aspects of an optically thick fluid it seems to be appeared in the literature as studied by many authors. England and Emery [<xref ref-type="bibr" rid="scirp.4674-ref1">1</xref>] have investigated the thermal radiation effects of an optically thin gray gas bounded by a stationary plate. The hydromagnetic free convection flow with radiative heat transfer in a rotating and optically thin fluid has been investigated by Bestman and Adiepong [<xref ref-type="bibr" rid="scirp.4674-ref2">2</xref>] and Naroua et al. [<xref ref-type="bibr" rid="scirp.4674-ref3">3</xref>]. Soundalgakar and Takhar [<xref ref-type="bibr" rid="scirp.4674-ref4">4</xref>] considered the radiative free convictive flow of an optically thin gray gas past a semi-infinite vertical plate.Takher et al. [<xref ref-type="bibr" rid="scirp.4674-ref5">5</xref>] have studied the radiation effects on MED free convection flow of a radiating gas past a semi-infinite vertical plate. Radiation effects on mixed convection along an isothermal vertical plate were studied by Hossain and Takhar [<xref ref-type="bibr" rid="scirp.4674-ref6">6</xref>]. Raptis and Perdikis [<xref ref-type="bibr" rid="scirp.4674-ref7">7</xref>] studied the effects of thermal radiation and free convection flow past a moving vertical plate. Thermal radiation effects of an optically thin gray gas were studied by Raptis and Perdikis [<xref ref-type="bibr" rid="scirp.4674-ref8">8</xref>]. Muthukumarswamy and Ganeshan [<xref ref-type="bibr" rid="scirp.4674-ref9">9</xref>] have considered radiation effects on flow past an impulsively started infinite vertical plate with variable temperature. Ghosh and Pop [<xref ref-type="bibr" rid="scirp.4674-ref10">10</xref>] have studied thermal radiation of an optically thick gray gas in the presence of indirect natural convection. Recently, several studies on radiative heat transfer have been reported by Raptis et al. [<xref ref-type="bibr" rid="scirp.4674-ref11">11</xref>], Duwairi and duwairi [<xref ref-type="bibr" rid="scirp.4674-ref12">12</xref>], Vasil’ev and Nesterov [<xref ref-type="bibr" rid="scirp.4674-ref13">13</xref>], Duwairi [<xref ref-type="bibr" rid="scirp.4674-ref14">14</xref>], Quaf MEM [<xref ref-type="bibr" rid="scirp.4674-ref15">15</xref>], Ghosh [16,17], Zueco [<xref ref-type="bibr" rid="scirp.4674-ref18">18</xref>], Samad and Rahman [<xref ref-type="bibr" rid="scirp.4674-ref19">19</xref>] and Beg and Ghosh [<xref ref-type="bibr" rid="scirp.4674-ref20">20</xref>]. In the light of Ghosh and Pop [<xref ref-type="bibr" rid="scirp.4674-ref10">10</xref>] work it is stated that the effect of pressure on velocity remains present at <img src="7-4900018\e19c922d-69d9-48f3-b550-07d93fa7d855.jpg" /> for <img src="7-4900018\ed3b99a6-5145-446f-acc5-b5cdc7ee8667.jpg" /> so that the pressure rise region near the leading edge of the hot plate leads to increase the velocity .Thus it comes to a justification of this problem leading to a fact that the pressure becomes absent due to a stagnation point flow. Since a thin radiation boundary layer is formed due to an optically thick fluid it is considered that the temperature varies linearly along the hot plate so that the temperature field is depend on the thickness of the radiation boundary layer <img src="7-4900018\364cc29b-de05-4c0d-a219-651d02d3326b.jpg" /> where <img src="7-4900018\b057a855-d400-4462-accc-e7758f06a246.jpg" /> and the thickness of the radiation layer is considered to be unity.</p><p>Although the radiation boundary layer thickness depends on Reynolds number the aim of the present investigation of the problem is to a study of thermal radiation of an optically thick gray gas in taking into account of an unsteady flow of an incompressible viscous fluid occupying a semi-infinite region of space bounded by an infinite horizontal moving hot flat plate in the presence of indirect natural convection by way of induced pressure gradient. Since the temperature field depends on Reynolds number the wall temperature does not constant (<img src="7-4900018\67935598-80eb-4eb9-b637-e4d6882754f6.jpg" />constant) as the temperature varies along the plate and the recovery factor is determined by the Reynolds number. An uniform wall temperature (<img src="7-4900018\d29e570f-cf51-4606-8b6c-f067c3105d99.jpg" />constant) for an isothermal flat plate is fully understood if the value of Reynolds number is equal to 1. Thus it comes to a conclusion that since the temperature field depends on radiation layer thickness <img src="7-4900018\2af352fb-b928-45ad-bf8b-5e05413cf0c9.jpg" /> it is a decisive importance to an isothermal flat plate (<img src="7-4900018\9c9ab95e-c4b1-4eea-b268-888621e5c02c.jpg" />constant) with regard to a finite thickness (<img src="7-4900018\d273badc-5ff2-43c3-ae76-5c367a1dae58.jpg" />) [see Ghosh and Pop [<xref ref-type="bibr" rid="scirp.4674-ref10">10</xref>]. In our present problem, the temperature field depends on Reynolds number so that the problem is to be considered non-isothermal case (<img src="7-4900018\3f98f1dc-817b-4641-a789-60c75ae11196.jpg" />constant) and the problem turns into isothermal case (<img src="7-4900018\a736dd73-0714-4645-beed-214acf57c838.jpg" />constant) when the value of Reynolds number is equal to 1. An interesting feature of this problem is to be determined an indirect natural convection flow where the induced pressure gradient is considered to be zero at infinity.</p></sec><sec id="s2"><title>2. Formulation of the Problem and Its Solution</title><p>Consider the unsteady flow of a viscous incompressible fluid occupying a semi-infinite region of space bounded by an infinite horizontal plates moving with constant velocity <img src="7-4900018\35b7515b-95a7-4c5c-83f5-93c13d6d7e7c.jpg" /> with reference to indirect natural convection by way of induced pressure gradient. The flow is considered optically thick gray gas with indirect natural convection and radiation. We choose the cartesian coordinate system is such a way that x-axis is taken along the plate in the direction of the flow and y-axis is normal to it [see <xref ref-type="fig" rid="fig1">Figure 1</xref>]. The induced pressure gradient lies in x-direction to the origin of the flow parallel to the plate. All the fluid properties are considered constant expect the influence of density variation in the body force term. The radiation heat flux in the x-direction is considered negligible in comparison to the y-axis.</p><p>The momentum equations in component form can take the form</p><disp-formula id="scirp.4674-formula134141"><label>(1)</label><graphic position="anchor" xlink:href="7-4900018\89eb9726-7d50-48bd-97bf-f73a5a6751e9.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.4674-formula134142"><label>(2)</label><graphic position="anchor" xlink:href="7-4900018\aea8695f-d094-45ac-88eb-8a82c7b351dc.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="7-4900018\d4240351-af30-48a7-a6f0-490b6c434f35.jpg" /> is the fluids density, p the pressure, <img src="7-4900018\e4088dd8-53fa-4129-9997-5a83d36b1b75.jpg" />the co-</p><p>efficient of viscosity and g the acceleration due to gravity.</p><p>The equation of energy is</p><disp-formula id="scirp.4674-formula134143"><label>(3)</label><graphic position="anchor" xlink:href="7-4900018\089ab5f4-7315-4336-b592-e9ca56783a20.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="7-4900018\fc7a30ed-0fe3-4fc6-9b87-9a3aa922d01f.jpg" /> is the specific heat and k the thermal conductivity.</p><p>It is assumed that there is a temperature variation along the x-direction of the horizontal plate. The temperature of the flow can be written as</p><disp-formula id="scirp.4674-formula134144"><label>(4)</label><graphic position="anchor" xlink:href="7-4900018\4033a13f-0e48-4ce1-8a44-9d64c72c4d3e.jpg"  xlink:type="simple"/></disp-formula><p>where T is the temperature of the fluid, <img src="7-4900018\728f60e1-8e50-4b9e-b002-876b7dc392c3.jpg" />the temperature of the fluid far away the plate and <img src="7-4900018\102fa3b0-00fe-42c5-a184-5e2eebb28147.jpg" /> the dimensionless temperature and<img src="7-4900018\88c96ff2-517d-4a4a-a7f7-9de3131bb125.jpg" />.</p><p>The equation of state becomes</p><disp-formula id="scirp.4674-formula134145"><label>(5)</label><graphic position="anchor" xlink:href="7-4900018\7ed86eef-1b3e-4143-8ece-2e2e236e6a54.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="7-4900018\485aa9c8-25fe-4033-8e80-6ef56a79a84e.jpg" /> is the density of the fluid, <img src="7-4900018\ab743842-e127-4187-aec1-e40456d779bc.jpg" />the coefficient of thermal expansion and the other symbols have their usual meanings.</p><p>From (2) and (5) we have</p><disp-formula id="scirp.4674-formula134146"><label>(6)</label><graphic position="anchor" xlink:href="7-4900018\dc384038-9a4d-4aa6-9788-3357ef6304f6.jpg"  xlink:type="simple"/></disp-formula><p>Sine the temperature is uniform at infinity, it is reasonably assumed to be <img src="7-4900018\8f409bde-39ab-4948-bf4c-8d766dd24a00.jpg" /> as<img src="7-4900018\4203af47-47b3-48cf-ad5e-7afaa8287eb8.jpg" />. Thus <img src="7-4900018\5a750444-a89d-4d1d-93e9-2b4fcd28dcf6.jpg" /></p><p>is zero everywhere in the flow. Hence (6) becomes</p><disp-formula id="scirp.4674-formula134147"><label>(7)</label><graphic position="anchor" xlink:href="7-4900018\08e4f596-e545-41a0-a75f-2b6dcf38dcd8.jpg"  xlink:type="simple"/></disp-formula><p>On the use of (7), the Equation (1) becomes</p><disp-formula id="scirp.4674-formula134148"><label>(8)</label><graphic position="anchor" xlink:href="7-4900018\50ce9122-d08d-41cc-a511-7f36b2a31e3a.jpg"  xlink:type="simple"/></disp-formula><p>Using infinity conditions in (8), one find</p><p><img src="7-4900018\57051acd-ef09-465d-a387-ef805132a6fd.jpg" /></p><p>Hence the Equation (8) reduced to</p><disp-formula id="scirp.4674-formula134149"><label>(9)</label><graphic position="anchor" xlink:href="7-4900018\c0021e77-6ff9-4574-88c1-da4c3c252dc7.jpg"  xlink:type="simple"/></disp-formula><p>The initial and boundary conditions are</p><disp-formula id="scirp.4674-formula134150"><label>(10)</label><graphic position="anchor" xlink:href="7-4900018\6625c4cb-5385-4e8f-8266-aac66f73d008.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.4674-formula134151"><label>(11)</label><graphic position="anchor" xlink:href="7-4900018\eb0d0529-0cc3-4c9a-b226-06e66535c6f6.jpg"  xlink:type="simple"/></disp-formula><p>From (4), it is stated that the temperature of the flow is dependent on Reynolds number.</p><p>The dimensionless temperature with the help of (4), we get</p><disp-formula id="scirp.4674-formula134152"><label>(12)</label><graphic position="anchor" xlink:href="7-4900018\56df1940-f530-44da-bba0-f478fc63375e.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="7-4900018\3f45ed1a-610c-41be-bd07-f2e15e0d91a3.jpg" /> and <img src="7-4900018\5f9c7d72-f579-4f05-b48e-dbbe66f52f90.jpg" /> the Reynolds number.</p><p>In comparison to the study of Ghosh and Pop [<xref ref-type="bibr" rid="scirp.4674-ref10">10</xref>] with reference to the dimensionless temperature</p><p><img src="7-4900018\5ffbfdea-8ce4-4dc3-b2cf-abf48d1558d3.jpg" />, where δ the radiation layer thickness and the other symbols have their usual meanings with</p><p><img src="7-4900018\d380f849-fd43-434a-a083-a1b9e4e7f833.jpg" />(L is the characteristic length), it is rigorously stated that the radiation layer thickness depends on Reynolds number and the plate temperatures does not constant (<img src="7-4900018\a2bc9960-b98c-41a6-888f-6f90f421d3eb.jpg" />constant). For an isothermal plate (<img src="7-4900018\9535036e-a1d1-4e66-b619-eefdbcfe36e1.jpg" />constant), the thickness of the radiation layer should be taken finite value i.e.<img src="7-4900018\890f94e8-fc3e-45ea-89c2-6262e789d1ce.jpg" />. In this situation, Ghosh and Pop [<xref ref-type="bibr" rid="scirp.4674-ref10">10</xref>] have considered finite thickness of radiation layer with isothermal flat plate (<img src="7-4900018\3e2ed41b-5b65-4381-86e0-6a3ed5ffd323.jpg" />constant). The present investigation deals with non-isothermal, flat plate (<img src="7-4900018\a7f86125-53fc-4f6f-99e9-cc8d6ac12e4f.jpg" />constant) as the temperature varies along the plate and the recovery factor is determined by the Reynolds number. It seems to be understood that this problem turns into isothermal case (<img src="7-4900018\031bac85-050c-497f-a556-96e58d110e07.jpg" />constant) if the Reynolds number<img src="7-4900018\3d043cc2-2097-495b-ad89-1104911bdf72.jpg" />.</p><p>Introduce the dimensionless quantities</p><p><img src="7-4900018\4ff37110-342b-48c4-8e20-ddf1ca5c7cd2.jpg" /></p><p><img src="7-4900018\5fd86867-0224-4230-a4c9-3b3a6995c327.jpg" /></p><disp-formula id="scirp.4674-formula134153"><label>(13)</label><graphic position="anchor" xlink:href="7-4900018\3a9f5c41-e89b-49d8-b351-532f81388530.jpg"  xlink:type="simple"/></disp-formula><p>where<img src="7-4900018\3c810350-bdbe-4946-befd-5fbdf248ec25.jpg" />, <img src="7-4900018\8f0749a3-33c2-4db5-ac25-d75a20a10b1c.jpg" />, <img src="7-4900018\2e62c9b0-a387-43b2-b63f-ee26e38583a9.jpg" />, k, g and <img src="7-4900018\887d51b1-e19c-4ea3-a0de-b982bff78fba.jpg" /> are, respectively, the coefficient of viscosity, kinemetic coefficient of viscosity, specific heat at constant pressure, thermal conductivity, gravitational acceleration and the coefficient of thermal expansion and the other symbols have their usual meanings.</p><p>On the use of (13), the Equation (9) becomes</p><disp-formula id="scirp.4674-formula134154"><label>(14)</label><graphic position="anchor" xlink:href="7-4900018\a37bdae6-fe69-4637-8106-f7440d71ada4.jpg"  xlink:type="simple"/></disp-formula><p>The radiation flux vector can be found from Isachenko et al. [<xref ref-type="bibr" rid="scirp.4674-ref21">21</xref>], Equations (16)-(38), page 382 and its formula is derived on the basis of the diffusion concept of radiation heat transfer in the following way:</p><disp-formula id="scirp.4674-formula134155"><label>(15)</label><graphic position="anchor" xlink:href="7-4900018\a4caf437-2b7d-4b5c-b4fd-6fdc76617461.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="7-4900018\0db15f37-4ae9-429b-a024-518c112ec854.jpg" /> and <img src="7-4900018\bec47d8f-2930-4e86-b714-fa82da0ebbf3.jpg" /> are, respectively, the Stefan-Boltzman constant and the spectral mean absorption coefficient of the medium.</p><p>It is assumed that the temperature differences within the flow are sufficiently small such that <img src="7-4900018\e97d0cc6-27bb-439a-a6d3-7e500af6157a.jpg" /> may be regarded as a linear function of the temperature. It can be established by expanding <img src="7-4900018\fa1333ee-45a8-4391-9134-5d7f148fe67b.jpg" /> i.e. a Taylor series about <img src="7-4900018\cfe709ed-e2ff-41f9-8991-91d7a1a7524f.jpg" /> and neglecting higher order term. Therefore, <img src="7-4900018\3abaab8b-580b-43e4-b195-e03b27bd1d21.jpg" />can be expressed in the following form</p><disp-formula id="scirp.4674-formula134156"><label>(16)</label><graphic position="anchor" xlink:href="7-4900018\725a4eb2-6ab4-4baf-9d56-731b1109c21b.jpg"  xlink:type="simple"/></disp-formula><p>Using Equations (15) and (16), the energy Equation (3) can be written in a dimensionless form subject to (13) such as</p><disp-formula id="scirp.4674-formula134157"><label>(17)</label><graphic position="anchor" xlink:href="7-4900018\bbc0f4f3-4747-4997-a38e-3d4821f7a82e.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="7-4900018\388f197a-46d2-4375-9b7f-0952d8f7b7bd.jpg" /> is the radiation paeameter.</p><p>The corresponding boundary conditions are</p><disp-formula id="scirp.4674-formula134158"><label>(18)</label><graphic position="anchor" xlink:href="7-4900018\9faf611f-6be4-457d-8dd2-08d98513205e.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.4674-formula134159"><label>(19)</label><graphic position="anchor" xlink:href="7-4900018\37286538-d401-4e51-8c02-ea99cf94ea0d.jpg"  xlink:type="simple"/></disp-formula><p>The solutions for the velocity and temperature distributions can be obtained by applying Laplace transform technique subject to the boundary conditions (18) and (19) together with the Equations (14) and (17) become</p><disp-formula id="scirp.4674-formula134160"><label>(20)</label><graphic position="anchor" xlink:href="7-4900018\979e2ffe-fac5-4ff5-89df-7a085f46a799.jpg"  xlink:type="simple"/></disp-formula><p>and</p><disp-formula id="scirp.4674-formula134161"><label>(21)</label><graphic position="anchor" xlink:href="7-4900018\6e03b723-abca-4b37-bb40-cf2eae54dd14.jpg"  xlink:type="simple"/></disp-formula><p>where</p><disp-formula id="scirp.4674-formula134162"><label>(21a)</label><graphic position="anchor" xlink:href="7-4900018\a62726ab-e133-4d54-8ae3-51725420b8ed.jpg"  xlink:type="simple"/></disp-formula><p>We shall now discuss some particular cases of interest Case I: In the absence of radiation parameter <img src="7-4900018\ee0ad4a2-343e-4952-927c-17f31f62092e.jpg" /> and the prandtl number<img src="7-4900018\884b01fb-909b-43d5-b3d6-764f8d2783b2.jpg" />, the solutions (20) and (21) reduce to</p><disp-formula id="scirp.4674-formula134163"><label>(22)</label><graphic position="anchor" xlink:href="7-4900018\edece200-0b19-41e6-a680-5bdd095a2f15.jpg"  xlink:type="simple"/></disp-formula><p>and</p><disp-formula id="scirp.4674-formula134164"><label>(23)</label><graphic position="anchor" xlink:href="7-4900018\85684f83-0989-4304-a72b-cdf1310414d7.jpg"  xlink:type="simple"/></disp-formula><p>Case II: In the absence of radiation temperature</p><p>(<img src="7-4900018\8c3e6645-e97a-42df-b481-2baa6341d55b.jpg" />) and the pressure gradient <img src="7-4900018\2f3055ee-3a36-4763-a89f-509989aa95dc.jpg" /> the Equations (1)-(3) transform into a flat plate at zero incidence so that the velocity and the temperature fields are identical when the prandtl number<img src="7-4900018\de200497-2109-4a88-8bfa-0b077b096ef3.jpg" />.</p></sec><sec id="s3"><title>3. Discussion and Results</title><p>The graphical representations of numerical results with different parameters<img src="7-4900018\13b55063-a346-4ea7-93ab-f254c4f59993.jpg" />, <img src="7-4900018\5cad1e6b-d259-4edd-b61e-006f6f81b5b7.jpg" />, <img src="7-4900018\ff576318-cdec-42c4-a08f-72fcc12ecee1.jpg" />, <img src="7-4900018\f848d531-f506-4c9f-9166-727e88a807af.jpg" />and <img src="7-4900018\777ec9f0-f65c-4490-8931-dd53812ed35b.jpg" /> for the velocity and temperature distributions are plotted against <img src="7-4900018\84e0a4b1-89a4-4764-961a-f717b7381cb2.jpg" /> in Figures 2-8. There is steep decline from the wall for all profiles in Figures 2-8 and no velocity and temperature overshoot. The profiles of spatial dimensionless velocity <img src="7-4900018\eb93b349-ae27-493c-b708-0a819842d034.jpg" /> with distance from the wall, at various time <img src="7-4900018\b5cc4d94-9b9e-4736-bd2c-bafb2db467db.jpg" /> are shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>. As time, <img src="7-4900018\a8f89cf7-46d0-44d6-83a5-4049d3a49d96.jpg" />, increases from 0.02, 0.04 to 0.08. we observed that the velocity <img src="7-4900018\34ff9439-5983-49b6-b781-7ca66ed8c2d8.jpg" /> is increased markedly. With time in <xref ref-type="fig" rid="fig2">Figure 2</xref> the flow is therefore, accelerate in the downward direction. <xref ref-type="fig" rid="fig3">Figure 3</xref> reveals that the velocity <img src="7-4900018\3c3e978d-dbe2-4866-8eee-8657ee4e3419.jpg" /> slightly increases with increase in radiation parameter<img src="7-4900018\c3e19be3-6dd0-46b0-a0ca-ef5f045e7431.jpg" />. The radiation conduction parameter <img src="7-4900018\6ddad826-475e-4c0b-aefa-7cff047496c3.jpg" /> defines the relative contribution of radiation heat transfer to thermal conduction transfer. By applying Stefan-Boltzman constant for an optically dense medium it is stated from <xref ref-type="fig" rid="fig3">Figure 3</xref> that an increase in radiation parameter <img src="7-4900018\a9572eda-7f04-493f-bcc1-ae15afea3fa1.jpg" /> leads to a slightly rise in velocity <img src="7-4900018\c60d7d35-bc7c-4d11-8b2f-17cbf8ddf50a.jpg" /> for any value of<img src="7-4900018\4c20a345-ade2-433f-ae6a-646d2685aeef.jpg" />. It is interesting to note that in a pressure rise region a slightly increase in velocity <img src="7-4900018\3b64acc2-371f-46f5-ae40-539d16244b29.jpg" /> is a remarkable feature of an optically thick (dense) medium. It is shown from <xref ref-type="fig" rid="fig4">Figure 4</xref> that an increase in Prandtl number <img src="7-4900018\4a1c6ecc-e183-479d-b0d3-e1613ad22bfe.jpg" /> leads to decrease the velocity<img src="7-4900018\3280b286-05af-4c1f-9495-56f2662cc3eb.jpg" />. Usually the value of Prandtl number <img src="7-4900018\c2ab3bea-4108-4137-abe9-89ecec2ab1d1.jpg" /> determines the highly ionized gas. In <xref ref-type="fig" rid="fig4">Figure 4</xref> it reveals that the velocity <img src="7-4900018\554b038e-c501-44b3-bf8a-d3413e4a8544.jpg" /> always decreases with increase in prandtl number <img src="7-4900018\298180c7-19f1-4369-87a6-d5c90d2a0066.jpg" /> for tri-atomic gas of its optical measurement. It is noticed from <xref ref-type="fig" rid="fig5">Figure 5</xref> that the velocity <img src="7-4900018\06dccb93-8003-4a2f-92d8-ce4981e3ff94.jpg" /> increases with increase in Grashof number<img src="7-4900018\52abd132-1e94-4c93-b01f-eb42b3e45f74.jpg" />. This situation reveals that the buoyancy force accelerates the velocity field and no flow reversal occurs to prevent separation. Figures 6 and 7 demonstrate that the temperature <img src="7-4900018\d5fe8041-3711-4066-8528-98c6cda9345e.jpg" /> increases with increase in either time <img src="7-4900018\b9b6561b-c85e-43f8-b9b6-82d4e7e9fc82.jpg" /> or radiation parameter<img src="7-4900018\de05e947-a979-43d2-ac82-ea5390a59129.jpg" />. <xref ref-type="fig" rid="fig8">Figure 8</xref> shows that an increase in Prandtl number <img src="7-4900018\d4b64b42-8b34-490a-88ce-3e1658b9f782.jpg" /> leads to fall the temperature. In relevance to the physical situation of interest it reveals that the temperature decreases with an increase in Prandtl number <img src="7-4900018\71705d86-54e8-445e-af34-34a4b1f10d38.jpg" /> for highly ionized gas.</p></sec><sec id="s4"><title>REFERENCES</title></sec></body><back><ref-list><title>References</title><ref id="scirp.4674-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">W. G. England and A. F. Emery, “Thermal Radiation Effects on the Laminear Free Convection Boundary Layer of an Absorbing Gas,” Journal of Heat Transfer, Vol. 91, 1969, pp. 37-44. </mixed-citation></ref><ref id="scirp.4674-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">A. R. Bestman and S. K. Adiepong, “Unsteady Hydro- magnetic Free-Convection Flow with Radiation Heat Transfer in a Rotating Fluid,” Astrophysics and Space Science, Vol. 143, No. 1, 1988, pp. 73-80. 
doi:10.1007/BF00636756</mixed-citation></ref><ref id="scirp.4674-ref3"><label>3</label><mixed-citation publication-type="other" xlink:type="simple">H. Naroua, P. C. Ram, A. S. Sambo and H. S. Takhar, “Finite Element Analysis of Natural Convection Flow in a Rotating Fluid with Radiative Heat Transfer,” Journal of Magnetohydrodynamics and Plasma Research, Vol. 7, No. 4, 1998, pp. 257-274.</mixed-citation></ref><ref id="scirp.4674-ref4"><label>4</label><mixed-citation publication-type="other" xlink:type="simple">V. M. Soundalgekar and H. S. Takhar, “Radiation Effects on Free Convection Flow past a Semi-Infinite Vertical Plate,” Modelling, Measurement and Control, Vol. B51, 1993, pp. 31-40.</mixed-citation></ref><ref id="scirp.4674-ref5"><label>5</label><mixed-citation publication-type="other" xlink:type="simple">H. S. Takhar, R. S. S. Gorla and V. M. Soundalgekar, “Radiation Effects on MED Free Convection Flow of a Radiating Gas Past a Semi-Infinite Vertical Plate,” Inter- national Journal of Numerical Methods for Heat &amp; Fluid Flow, Vol. 6, 1996, pp. 77-83.</mixed-citation></ref><ref id="scirp.4674-ref6"><label>6</label><mixed-citation publication-type="other" xlink:type="simple">M. A. Hossain and H. S. Takhar, “Radiation Efeects on Mixed Convection along a Vertical Plate with Uniform Surface Temperature,” Heat and Mass Transfer, Vol. 31, No. 4, 1996, pp. 243-248. doi:10.1007/BF02328616</mixed-citation></ref><ref id="scirp.4674-ref7"><label>7</label><mixed-citation publication-type="other" xlink:type="simple">A. Raptis and C. Perdikis, “Radiation and Free Con- vection Flow past a Moving Plate,” Applied Mechanics and Engineering, Vol. 4, No. 4, 1990, pp. 817-821.</mixed-citation></ref><ref id="scirp.4674-ref8"><label>8</label><mixed-citation publication-type="other" xlink:type="simple">A. Raptis and C. Perdikis, “Thermal Radiation of an Optically Thin Gray Gas,” International Journal of Applied Mechanics and Engineering, Vol. 8, No. 1, 2003, pp. 131-134.</mixed-citation></ref><ref id="scirp.4674-ref9"><label>9</label><mixed-citation publication-type="other" xlink:type="simple">R. Madhucumaraswamy and P. Ganesan, “Radiation Effects on Flow past an Impulsively Started Infinite Ver- tical Plate with Variable Temperature,” International Journal of Applied Mechanics and Engineering, Vol. 8, No. 1, 2003, pp. 125-129.</mixed-citation></ref><ref id="scirp.4674-ref10"><label>10</label><mixed-citation publication-type="other" xlink:type="simple">S. K. Ghosh and I. Pop, “Thermal Radiation of an Opti- cally Thick Gray Gas in the Presence of Indirect Natural Convection,” International Journal of Fluid Mechanics Research, Vol. 34, No. 6, 2007, pp. 515-520.</mixed-citation></ref><ref id="scirp.4674-ref11"><label>11</label><mixed-citation publication-type="other" xlink:type="simple">A. Raptis, C. Perdikis and H. S. Takhar, “Effect of Ther- mal Radiation on MHD Flow,” Applied Mathematics and Computation, Vol. 153, No. 3, 2004, pp. 645-649.  
doi:10.1016/S0096-3003(03)00657-X</mixed-citation></ref><ref id="scirp.4674-ref12"><label>12</label><mixed-citation publication-type="other" xlink:type="simple">H. M. Duwairi and R. M. Duwairi, “Thermal Radiation Effect on Mhd Rayleigh Flow with Constant Surface Heat Flux,” Heat and Mass Transfer, Vol. 41, No. 1, 2005, pp. 51-57.</mixed-citation></ref><ref id="scirp.4674-ref13"><label>13</label><mixed-citation publication-type="other" xlink:type="simple">E. N. Vasil’ev and D. A. Nesterov, “The Effect of Ra- diative — Convective Heat Transfer on the Formation of Current Layer,” High Temperature, Vol. 43, No. 3, 2005, pp. 396-403.</mixed-citation></ref><ref id="scirp.4674-ref14"><label>14</label><mixed-citation publication-type="other" xlink:type="simple">H. M. Duwairi, “Viscous and Joule Heating Effects on Forced Convection Flow From Radiate Isothermal Porous Surface,” International Journal of Numerical methods Heat Fluid Flow, Vol. 15, No. 5, 2005, pp. 429-440.  
doi:10.1108/09615530510593620</mixed-citation></ref><ref id="scirp.4674-ref15"><label>15</label><mixed-citation publication-type="other" xlink:type="simple">M. E. M. Quaf, “Exact Solution of Thermal Radiation on Mhd Flow over a Stretching Porous Sheet,” Applied Ma- thematics and Computation, Vol. 170, No. 2, 2005, pp. 1117-1125.</mixed-citation></ref><ref id="scirp.4674-ref16"><label>16</label><mixed-citation publication-type="other" xlink:type="simple">S. K. Ghosh, “Radiative Heat Transfer Aspect of an Optically Thick Gray Gas in the Presence of a Magnetic Field,” International Journal of Applied Mechanics and Engineering, Vol. 12, No. 3, 2007, pp. 849-855.</mixed-citation></ref><ref id="scirp.4674-ref17"><label>17</label><mixed-citation publication-type="other" xlink:type="simple">S. K. Ghosh, “Radiative Heat Transfer Aspect of an Opti- cally Thick Gray Gas in the Presence of a Magnetic Field,” International Journal of Applied Mechanics and Engineering, Vol. 12, No. 4, 2007, pp. 1181.</mixed-citation></ref><ref id="scirp.4674-ref18"><label>18</label><mixed-citation publication-type="other" xlink:type="simple">J. Zueco, “Network Simulation Method Applied to Ra- diation and Viscous Dissipation Effects on MHD Un- steady Free Convection Over a Vertical Porous Plate,” Applied Mathematical Modelling, Vol. 31, No. 9, 2007, pp. 2019-2033.</mixed-citation></ref><ref id="scirp.4674-ref19"><label>19</label><mixed-citation publication-type="other" xlink:type="simple">M. A. Samad and M. M. Rahman, “Thermal Radiation Interaction with Unsteady MHD Flow past a Vertical Porous Plate Immersed in a Porous Medium,” Journal of Naval Architecture and Marine Engineering, Vol. 3, No. 1, 2006, pp. 7-14.</mixed-citation></ref><ref id="scirp.4674-ref20"><label>20</label><mixed-citation publication-type="other" xlink:type="simple">O. A. Beg and S. K. Ghosh, “Analytical Study of Magne- tohydrodynamic Radiation — Convection with Surface Temperature Oscillation and Secondary Flow Effects,” International Journal of Applied Mathematics and Me- chanics, Vol. 6, No. 6, 2010, pp. 1-22.</mixed-citation></ref><ref id="scirp.4674-ref21"><label>21</label><mixed-citation publication-type="other" xlink:type="simple">V. P. Isachenko, V. A. Osipova and A. S. Sukomel, “Heat Transfer,” Mir Publishers, Moscow, 1969, pp. 341-451.</mixed-citation></ref></ref-list></back></article>