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	<title>www.thepetrosolutions.com | Hamzaali1999 | Activity</title>
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				<title>Hamzaali1999 started the topic Temperatures and LHSV at Naphtha Hydrotreater Reactor in the forum Process Operations</title>
				<link>https:/forums/topic/naphtha-hydrotreater/</link>
				<pubDate>Fri, 14 Jul 2023 00:42:17 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hello, I hope you all are fine.</p>
<p>My question is,<br />
Is there is any importance of reactor inlet temperature while calculating LHSV ? As in LHSV formula/equation there is no any temperature term. Simply we calculated LHSV as,</p>
<p>LHSV = volume of charge per hour / volume of catalyst</p>
<p>As during operation, the reactor inlet temperature is fixed lets&hellip;<span class="activity-read-more" id="activity-read-more-3311"><a href="https:/forums/topic/naphtha-hydrotreater/" rel="nofollow ugc">Read more</a></span></p>
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				<guid isPermaLink="false">227ece3d062dc79980a4c533f3f501e1</guid>
				<title>Hamzaali1999 replied to the topic Job roles of a Chemical Engineer in an oil refinery in the forum Career Counseling</title>
				<link>https:/forums/topic/job-roles-of-a-chemical-engineer-in-an-oil-refinery/#post-2897</link>
				<pubDate>Sun, 08 Jan 2023 05:04:57 +0000</pubDate>

									<content:encoded><![CDATA[<p>1) For an plant operations engineer which skills are in demand nationally and internationally ?<br />
2) What are the basic skills of an plant operation engineer ?<br />
3) How plant operations engineer move towards new role/title like production planning engineer &amp; project engineer ?<br />
3) What skills are in demand for project/production planning engineer&hellip;<span class="activity-read-more" id="activity-read-more-3303"><a href="https:/forums/topic/job-roles-of-a-chemical-engineer-in-an-oil-refinery/#post-2897" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 started the topic Troubleshooting &#038; Inspection &#038; Understanding in the forum Process Operations</title>
				<link>https:/forums/topic/troubleshooting-inspection-understanding/</link>
				<pubDate>Sun, 08 Jan 2023 05:04:39 +0000</pubDate>

									<content:encoded><![CDATA[<p>Dear Sir,</p>
<p>I want to understand troubleshooting of pumps (centrifugal pump) &amp; compressors (reciprocating/centrifugal).</p>
<p>1) How to inspect these equipment as an operation engineer ? What things one need to check and monitor ?</p>
<p>2) A pump used to pump the fluid having RVP of 1.8 psi. Can we pump a fluid having RVP of 6-9 psi by using this same&hellip;<span class="activity-read-more" id="activity-read-more-3302"><a href="https:/forums/topic/troubleshooting-inspection-understanding/" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 started the topic Height Of Distillation Column (De-Butanizer) in the forum Engineering Students</title>
				<link>https:/forums/topic/height-of-distillation-column-de-butanizer/</link>
				<pubDate>Tue, 17 Aug 2021 07:39:16 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi,</p>
<p>I hope you all are fine and doing great. </p>
<p>Currently I am designing my final year design project. I am designing catalytic reforming plant and process used is CCR by UOP. I almost design all major equipment. I copes with some problem while designing the distillation column and also called de-butainzer. My questions are below;</p>
<p>1) I&hellip;<span class="activity-read-more" id="activity-read-more-518"><a href="https:/forums/topic/height-of-distillation-column-de-butanizer/" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 started the topic Pipeline Of Pump in the forum Engineering Students</title>
				<link>https:/forums/topic/pipeline-of-pump/</link>
				<pubDate>Tue, 17 Aug 2021 07:39:10 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi </p>
<p>I hope you all are fine and doing great </p>
<p>I am designing centrifugal pump. The only data I have is pressure difference means inlet &amp; outlet pressures and temperatures. I didn&#8217;t know pipe diameter, velocity, area etc&#8230;I performed discharge calculations and for that I choose schedule 40 pipe with 3.5 inch nominal pipe size. Now for suction&hellip;<span class="activity-read-more" id="activity-read-more-517"><a href="https:/forums/topic/pipeline-of-pump/" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 started the topic Designing of Fired Heater in the forum Engineering Students</title>
				<link>https:/forums/topic/designing-of-fired-heater/</link>
				<pubDate>Wed, 17 Mar 2021 18:16:36 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi<br />
Hope so you all are fine </p>
<p>Kindly guide me about fired heater designing. How should I start my designing </p>
<p>As I studied about fired heater designing is that we have to assume several parameters and values like dimensions tube length and diameter, average radiant flux, efficiency of heater and radiant zone. </p>
<p>I am totally confused if you are&hellip;<span class="activity-read-more" id="activity-read-more-449"><a href="https:/forums/topic/designing-of-fired-heater/" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 started the topic Heavy Naphtha Feed Average Molecular Weight in the forum Engineering Students</title>
				<link>https:/forums/topic/heavy-naphtha-feed-average-molecular-weight/</link>
				<pubDate>Fri, 05 Mar 2021 05:21:05 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi<br />
Hope so you all are fine</p>
<p>I am confused in calculating average molecular weight of heavy Naphtha Feed that comes from NHT Unit and flow towards reforming unit.</p>
<p>As the formula for average molecular weight of gases is</p>
<p>M.W(avg) = sum of (mole fraction of components x molecular weight of components)</p>
<p>So let suppose I calculated the&hellip;<span class="activity-read-more" id="activity-read-more-421"><a href="https:/forums/topic/heavy-naphtha-feed-average-molecular-weight/" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 replied to the topic Catalyst regeneration (Cycle Max regenerator) in the forum Engineering Students</title>
				<link>https:/forums/topic/catalyst-regeneration-cycle-max-regenerator/#post-1207</link>
				<pubDate>Sat, 27 Feb 2021 12:53:03 +0000</pubDate>

									<content:encoded><![CDATA[<p>Thanks alot sir &#x1f642;</p>
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				<guid isPermaLink="false">54e0ebc54a48ab6d747d0db8a3d68af6</guid>
				<title>Hamzaali1999 started the topic Catalyst regeneration (Cycle Max regenerator) in the forum Engineering Students</title>
				<link>https:/forums/topic/catalyst-regeneration-cycle-max-regenerator/</link>
				<pubDate>Fri, 26 Feb 2021 22:12:40 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi<br />
My question is </p>
<p>How much time is needed to regenerate the catalyst in CCR process. Let suppose if it took 10 min or 20 min then there will be stopagge of production for 20 min ? </p>
<p>Kindly guide me in detail </p>
<p>Thanks </p>
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				<title>Hamzaali1999 started the topic Modification in CCR in the forum Engineering Students</title>
				<link>https:/forums/topic/modification-in-ccr/</link>
				<pubDate>Fri, 26 Feb 2021 22:12:17 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi<br />
My question is that </p>
<p>What modification we can do in CCR process that is currently adopted by almost all refineries? </p>
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				<guid isPermaLink="false">cfa549b03f23702af2af4b31aa728aab</guid>
				<title>Hamzaali1999 started the topic Catalytic Reforming in the forum Engineering Students</title>
				<link>https:/forums/topic/catalytic-reforming/</link>
				<pubDate>Fri, 26 Feb 2021 18:56:57 +0000</pubDate>

									<content:encoded><![CDATA[<p>Hi<br />
Hope so you all are fine and doing great<br />
My questions are;</p>
<p><strong>1) What do you mean by the term &#8220;dump and screen of catalyst&#8221;?</strong></p>
<p><strong>2) What do you mean by cycle length and severity of process ( low severity operation and high severity operation) in catalytic reforming?</strong></p>
<p><strong>3) What is difference between in situ and ex situ catalyst&hellip;</strong><span class="activity-read-more" id="activity-read-more-409"><a href="https:/forums/topic/catalytic-reforming/" rel="nofollow ugc">Read more</a></span></p>
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				<title>Hamzaali1999 replied to the topic Comparison of reforming processes in the forum Engineering Students</title>
				<link>https:/forums/topic/comparison-of-reforming-processes/#post-838</link>
				<pubDate>Sun, 22 Nov 2020 09:34:16 +0000</pubDate>

									<content:encoded><![CDATA[<p>A.o.a<br />
Kindly very my document which contains the comparison of reforming processes. If I made any mistake then kindly tell me.</p>
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				<guid isPermaLink="false">6f1a444f4245bb3a4ca09dbc981491e7</guid>
				<title>Hamzaali1999 started the topic Comparison of different reforming process in the forum Engineering Students</title>
				<link>https:/forums/topic/comparison-of-different-reforming-process/</link>
				<pubDate>Sun, 22 Nov 2020 08:12:17 +0000</pubDate>

									<content:encoded><![CDATA[<p>A.o.a<br />
Kindly very my document which contains the comparison of reforming processes. If I made any mistake then kindly tell me.</p>
<p>Secondly<br />
<strong>these are the justification for selecting UOP CCR Platforming Process </strong></p>
<p>Following are the justification for selecting “CCR Platforming Process”</p>
<p>1)This process used Pt/Al203 which produce maximum yield of des&hellip;<span class="activity-read-more" id="activity-read-more-345"><a href="https:/forums/topic/comparison-of-different-reforming-process/" rel="nofollow ugc">Read more</a></span></p>
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				<guid isPermaLink="false">1d57f98f193f3322a3171424d88e4d64</guid>
				<title>Hamzaali1999 started the topic Comparison of reforming processes in the forum Engineering Students</title>
				<link>https:/forums/topic/comparison-of-reforming-processes/</link>
				<pubDate>Sat, 21 Nov 2020 19:33:14 +0000</pubDate>

									<content:encoded><![CDATA[<p>A.o.a<br />
Kindly very my document which contains the comparison of reforming processes. If I made any mistake then kindly tell me.</p>
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				<title>Hamzaali1999 started the topic Properties of Gasoline in the forum Product Quality</title>
				<link>https:/forums/topic/properties-of-gasoline/</link>
				<pubDate>Sat, 03 Oct 2020 04:57:40 +0000</pubDate>

									<content:encoded><![CDATA[<p>My question is that what are properties of gasoline </p>
<p>How many methods are there for gasoline production </p>
<p>Any reference for finding gasoline properties</p>
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				<guid isPermaLink="false">0e5b241949b852b5527193f69b2c880e</guid>
				<title>Hamzaali1999 started the topic CCR Plateforming in the forum Engineering Students</title>
				<link>https:/forums/topic/ccr-plateforming/</link>
				<pubDate>Wed, 15 Apr 2020 08:33:04 +0000</pubDate>

									<content:encoded><![CDATA[<p>Sir can you tell me about feed entering in CCR plateforming unit<br />
Means it&#8217;s flow rate entering for material balance and energy balance<br />
Secondly is about it&#8217;s reactor which reactors we use ?<br />
Means fixed bed, packed bed, fluidized bed, stacked bed ? </p>
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				<title>Hamzaali1999 started the topic Feed composition of Alkylation plant in the forum Engineering Students</title>
				<link>https:/forums/topic/feed-composition-of-alkylation-plant/</link>
				<pubDate>Tue, 14 Apr 2020 17:25:54 +0000</pubDate>

									<content:encoded><![CDATA[<p>Sir I understand that very well. But I want to know the composition of Alkylation plant feed and I totally confused about it&#8217;s composition. I am doing my FYDP on Alkylation plant so for this I want to know the exact composition of feed </p>
<p>Thanks </p>
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				<guid isPermaLink="false">82dc19b1e7d65264aed834e90c1267db</guid>
				<title>Hamzaali1999 started the topic Alkylation unit in the forum Engineering Students</title>
				<link>https:/forums/topic/alkylation-unit/</link>
				<pubDate>Mon, 13 Apr 2020 20:31:43 +0000</pubDate>

									<content:encoded><![CDATA[<p>Sir I want some guidline about Alkylation unit. First of I want to ask it&#8217;s feasibility in Pakistan. Can we install the project in pakistan&#8217;s refineries. If yes then why refineries doesn&#8217;t install that unit even this unit give high octane component of gasoline blending even there is zero sulphur aromatics which are toxic? </p>
<p>Second question is&hellip;<span class="activity-read-more" id="activity-read-more-19"><a href="https:/forums/topic/alkylation-unit/" rel="nofollow ugc">Read more</a></span></p>
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