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		<id>http://www.colloquiam.com/wd/index.php?action=history&amp;feed=atom&amp;title=Wenlong_et_al_2011a</id>
		<title>Wenlong et al 2011a - Revision history</title>
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		<updated>2026-07-02T23:42:32Z</updated>
		<subtitle>Revision history for this page on the wiki</subtitle>
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	<entry>
		<id>http://www.colloquiam.com/wd/index.php?title=Wenlong_et_al_2011a&amp;diff=181494&amp;oldid=prev</id>
		<title>Scipediacontent: Scipediacontent moved page Draft Content 479732105 to Wenlong et al 2011a</title>
		<link rel="alternate" type="text/html" href="http://www.colloquiam.com/wd/index.php?title=Wenlong_et_al_2011a&amp;diff=181494&amp;oldid=prev"/>
				<updated>2021-01-21T12:02:54Z</updated>
		
		<summary type="html">&lt;p&gt;Scipediacontent moved page &lt;a href=&quot;/public/Draft_Content_479732105&quot; class=&quot;mw-redirect&quot; title=&quot;Draft Content 479732105&quot;&gt;Draft Content 479732105&lt;/a&gt; to &lt;a href=&quot;/public/Wenlong_et_al_2011a&quot; title=&quot;Wenlong et al 2011a&quot;&gt;Wenlong et al 2011a&lt;/a&gt;&lt;/p&gt;
&lt;table class=&quot;diff diff-contentalign-left&quot; data-mw=&quot;interface&quot;&gt;
				&lt;tr style='vertical-align: top;' lang='en'&gt;
				&lt;td colspan='1' style=&quot;background-color: white; color:black; text-align: center;&quot;&gt;← Older revision&lt;/td&gt;
				&lt;td colspan='1' style=&quot;background-color: white; color:black; text-align: center;&quot;&gt;Revision as of 12:02, 21 January 2021&lt;/td&gt;
				&lt;/tr&gt;&lt;tr&gt;&lt;td colspan='2' style='text-align: center;' lang='en'&gt;&lt;div class=&quot;mw-diff-empty&quot;&gt;(No difference)&lt;/div&gt;
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		<author><name>Scipediacontent</name></author>	</entry>

	<entry>
		<id>http://www.colloquiam.com/wd/index.php?title=Wenlong_et_al_2011a&amp;diff=181493&amp;oldid=prev</id>
		<title>Scipediacontent: Created page with &quot; == Abstract ==  Condensate gas is mainly demonstrated by methane. However, it also contains a lot of heavier contents like C5 or C5+ and some non-hydrocarbon mixture as well...&quot;</title>
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				<updated>2021-01-21T12:02:50Z</updated>
		
		<summary type="html">&lt;p&gt;Created page with &amp;quot; == Abstract ==  Condensate gas is mainly demonstrated by methane. However, it also contains a lot of heavier contents like C5 or C5+ and some non-hydrocarbon mixture as well...&amp;quot;&lt;/p&gt;
&lt;p&gt;&lt;b&gt;New page&lt;/b&gt;&lt;/p&gt;&lt;div&gt;&lt;br /&gt;
== Abstract ==&lt;br /&gt;
&lt;br /&gt;
Condensate gas is mainly demonstrated by methane. However, it also contains a lot of heavier contents like C5 or C5+ and some non-hydrocarbon mixture as well (Mokhatab et al, 2006). After recovering from gas wells, condensate gas needs liquid separation, gas purification and condensate stabilization treatment in the processing plant to meet the quality requirements. Processing plants far away from the gas well with long distances of two-phase flow in one condensate gas pipeline will take less investment than adjacent process plant with two single phase pipelines which are dry gas pipeline and liquid phase pipeline (Li, 2008). If the operation temperature somewhere in the condensate gas pipeline is lower than the gas dew point, liquid condensation would occur, subjecting the pipeline to two phase flow (Potocnik, 2010). While gas and its condensate flow simultaneously, mass transfer takes place continuously due to the change in pressure and temperature conditions. This leads to compositional changes and associated fluid property changes and also makes the hydraulic and thermal calculations of condensate gas more complex than normal gas. The condensate gas pipeline model which is established and solved based on the principle of fluid mechanics can simulate hydraulic and thermal parameters under various operation conditions. By means of technical support, this model is of great importance in the pipeline design and safety operation aspects (Mokhatab, 2009).&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Original document ==&lt;br /&gt;
&lt;br /&gt;
The different versions of the original document can be found in:&lt;br /&gt;
&lt;br /&gt;
* [http://www.intechopen.com/articles/show/title/modeling-and-simulation-for-steady-state-and-transient-pipe-flow-of-condensate-gas http://www.intechopen.com/articles/show/title/modeling-and-simulation-for-steady-state-and-transient-pipe-flow-of-condensate-gas]&lt;br /&gt;
&lt;br /&gt;
* [https://www.intechopen.com/citation-pdf-url/20171 https://www.intechopen.com/citation-pdf-url/20171] under the license cc-by-nc-sa&lt;br /&gt;
&lt;br /&gt;
* [http://www.intechopen.com/download/pdf/20171 http://www.intechopen.com/download/pdf/20171],&lt;br /&gt;
: [http://dx.doi.org/10.5772/23621 http://dx.doi.org/10.5772/23621]&lt;br /&gt;
&lt;br /&gt;
* [https://www.intechopen.com/books/thermodynamics-kinetics-of-dynamic-systems/modeling-and-simulation-for-steady-state-and-transient-pipe-flow-of-condensate-gas https://www.intechopen.com/books/thermodynamics-kinetics-of-dynamic-systems/modeling-and-simulation-for-steady-state-and-transient-pipe-flow-of-condensate-gas],&lt;br /&gt;
: [https://cdn.intechweb.org/pdfs/20171.pdf https://cdn.intechweb.org/pdfs/20171.pdf],&lt;br /&gt;
: [http://cdn.intechopen.com/pdfs-wm/20171.pdf http://cdn.intechopen.com/pdfs-wm/20171.pdf],&lt;br /&gt;
: [http://cdn.intechopen.com/pdfs/20171/InTech-Modeling_and_simulation_for_steady_state_and_transient_pipe_flow_of_condensate_gas.pdf http://cdn.intechopen.com/pdfs/20171/InTech-Modeling_and_simulation_for_steady_state_and_transient_pipe_flow_of_condensate_gas.pdf],&lt;br /&gt;
: [https://academic.microsoft.com/#/detail/1566026545 https://academic.microsoft.com/#/detail/1566026545]&lt;/div&gt;</summary>
		<author><name>Scipediacontent</name></author>	</entry>

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