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	<title>www.thepetrosolutions.com | Abu noor | Activity</title>
	<link>https://thepetrosolutions.com/members/dodge360l/activity/</link>
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	<description>Activity feed for Abu noor.</description>
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				<guid isPermaLink="false">978b1f588d3aaa4721467a21f2578705</guid>
				<title>Abu noor started the topic Bypassing diolefins reactor in DHT unit in the forum Hydroprocessing</title>
				<link>https:/forums/topic/diolefins-reactor-in-dht-unit/</link>
				<pubDate>Tue, 19 Oct 2021 10:43:28 +0000</pubDate>

									<content:encoded><![CDATA[<p>During replacement of diolefins reactor in DHT unit.We can bypass this reactor and continued cocker naphtha to DHT reactor?<br />
There is any impact to hydrotreater reactor and Fractionator column of we cutoff Cocker naphtha.we have SRGO and LCGO feed to hydrotreater reactor plus cocker naphtha after treated in diolefins reactor.<br />
I need your suggestions<br />
Thanks </p>
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				<guid isPermaLink="false">e9268b0059caf332c58f2e757ffd7d0b</guid>
				<title>Abu noor started the topic WABT changes while Feed Rate changes in hydrotreating unit in the forum Hydroprocessing</title>
				<link>https:/forums/topic/wabt-changes-while-feed-rate-changes/</link>
				<pubDate>Fri, 06 Aug 2021 10:31:42 +0000</pubDate>

									<content:encoded><![CDATA[<p>I want to adjust WABT while feed rate changes in diesel hydrotreater unit.for example start of Run WABT 330 how I can adjust.please share with me excel sheet for proper calculation and adjustment.</p>
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				<guid isPermaLink="false">c767a839c04b54d45084e13fa152d22a</guid>
				<title>Abu noor started the topic Sulfiding of Diolefins Reactor in Diesel Hydrotreating unit in the forum Hydroprocessing</title>
				<link>https:/forums/topic/diolefins-reactor-in-diesel-unit/</link>
				<pubDate>Sat, 26 Jun 2021 14:09:02 +0000</pubDate>

									<content:encoded><![CDATA[<p>In Diesel unit we have diolefins reactor it’s required both high temperature sulfiding and low temperature sulfiding or only low temperature sulfiding because we don’t have any hot source to increase the reactor inlet temperature more than 200 deg the preheater to the diolefins reactor is heated by fractionator bottoms?</p>
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				<guid isPermaLink="false">ebb04f42831965051537a6dc18ab7681</guid>
				<title>Abu noor started the topic Hydrocraker unit (two stages) conversion calculation in the forum Hydroprocessing</title>
				<link>https:/forums/topic/hydrocraker-unit-two-stages-conversion-calculation/</link>
				<pubDate>Sun, 13 Jun 2021 09:17:48 +0000</pubDate>

									<content:encoded><![CDATA[<p>How to make a calculation tag of conversion , recycle cut point and per pass conversion of hydrocracker without lab analysis ?</p>
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				<guid isPermaLink="false">d1182bae744d2afbd5029fc02d117496</guid>
				<title>Abu noor&#039;s profile was updated</title>
				<link>https://thepetrosolutions.com/activity/p/499/</link>
				<pubDate>Sun, 30 May 2021 15:56:30 +0000</pubDate>

				
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				<guid isPermaLink="false">ae06035d627816b1f3687ff28724e75e</guid>
				<title>Abu noor started the topic Feed Filters Pressure Control in Diesel Hydrotreating Unit in the forum Hydroprocessing</title>
				<link>https:/forums/topic/feed-filter-outlet-pressure-control/</link>
				<pubDate>Sun, 30 May 2021 15:55:13 +0000</pubDate>

									<content:encoded><![CDATA[<p>What’s the purpose of feed filter pressure control in diesel unit?</p>
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				<guid isPermaLink="false">7c47f25b5443a30be3b5570e41a33c12</guid>
				<title>Abu noor replied to the topic Diesel unit system pressure during sulfiding in the forum Hydroprocessing</title>
				<link>https:/forums/topic/diesel-unit-system-pressure-during-sulfiding/#post-1461</link>
				<pubDate>Sat, 24 Apr 2021 16:24:25 +0000</pubDate>

									<content:encoded><![CDATA[<p>Thanks Mr.Naser </p>
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				<guid isPermaLink="false">8c2adae75a76d506d83f91d6bfbdd122</guid>
				<title>Abu noor started the topic Diesel unit system pressure during sulfiding in the forum Hydroprocessing</title>
				<link>https:/forums/topic/diesel-unit-system-pressure-during-sulfiding/</link>
				<pubDate>Thu, 22 Apr 2021 17:29:38 +0000</pubDate>

									<content:encoded><![CDATA[<p>In diesel hydrotreating unit during sulfiding why we can not increase system pressure 100% up to normal operating pressure?</p>
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				<guid isPermaLink="false">e2c72e952cd564dcf66cad091f97dabf</guid>
				<title>Abu noor replied to the topic Long loop and short loop circulation on DHT in the forum Hydroprocessing</title>
				<link>https:/forums/topic/long-loop-and-short-loop-circulation-on-dht/#post-1454</link>
				<pubDate>Tue, 13 Apr 2021 18:52:58 +0000</pubDate>

									<content:encoded><![CDATA[<p>Thanks Mr.Nasser<br />
For fast response </p>
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				<guid isPermaLink="false">14eb040a84e7ab0c896de87e829374e9</guid>
				<title>Abu noor replied to the topic Long loop and short loop circulation on DHT in the forum Hydroprocessing</title>
				<link>https:/forums/topic/long-loop-and-short-loop-circulation-on-dht/#post-1449</link>
				<pubDate>Mon, 12 Apr 2021 14:50:05 +0000</pubDate>

									<content:encoded><![CDATA[<p>Thanks Mr.Nasir<br />
Once flushing is completed through system we can stop Fractionator pump which is used for internal circulation?<br />
Only we will keep long loop circulation if not why?</p>
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				<guid isPermaLink="false">5c811bb008054e0c9d7b626476dbe29c</guid>
				<title>Abu noor started the topic Long loop and short loop circulation on DHT in the forum Hydroprocessing</title>
				<link>https:/forums/topic/long-loop-and-short-loop-circulation-on-dht/</link>
				<pubDate>Sat, 10 Apr 2021 10:32:58 +0000</pubDate>

									<content:encoded><![CDATA[<p>What is the purpose of the cold, hot long loop circulation and short loop circulation on the hydrotreater unit?<br />
And we can use hot or cold long loop circulation?</p>
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				<title>Abu noor replied to the topic BMS Heaters Firing Control in the forum Energy Management</title>
				<link>https:/forums/topic/bms-heaters-firing-control/#post-1427</link>
				<pubDate>Tue, 06 Apr 2021 07:56:32 +0000</pubDate>

									<content:encoded><![CDATA[<p>As we discussed earlier here attached sketch for heaters firing control.</p>
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				<guid isPermaLink="false">003fac50b6831571944fdbec622b4e09</guid>
				<title>Abu noor started the topic Diesel Vacuum Driers in the forum Process Operations</title>
				<link>https:/forums/topic/diesel-vacuum-driers/</link>
				<pubDate>Sat, 03 Apr 2021 09:49:13 +0000</pubDate>

									<content:encoded><![CDATA[<p>I am looking for Start up, Shutdown and handover to maintenance diesel vacuum drier</p>
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				<guid isPermaLink="false">87c945e9515dd55ce980cbff23438092</guid>
				<title>Abu noor started the topic BMS Heaters Firing Control in the forum Energy Management</title>
				<link>https:/forums/topic/bms-heaters-firing-control/</link>
				<pubDate>Sat, 03 Apr 2021 09:48:25 +0000</pubDate>

									<content:encoded><![CDATA[<p>In BMS heaters which is better, more accurate,not hunting and good for turning?<br />
1.connected temperature controller with Fuel gas controller<br />
1 . Connected temperature with low selector.</p>
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				<guid isPermaLink="false">6650ad8afc6b4a74d9bfa587664d9d1b</guid>
				<title>Abu noor started the topic Heaters refractory dry out procedure in the forum Process Operations</title>
				<link>https:/forums/topic/heaters-refractory-dry-out/</link>
				<pubDate>Sun, 28 Mar 2021 17:43:32 +0000</pubDate>

									<content:encoded><![CDATA[<p>I need guidelines for heaters refractory dry out. How much temperature should be maximum and minimum? which media we can use inside the coil (steam, nitrogen, oil&#8230;.etc)or without media?</p>
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				<guid isPermaLink="false">fa61e358e7a0988edbc700b270a265fb</guid>
				<title>Abu noor replied to the topic Product stripper feed to fractionator furnace flow control in the forum Process Operations</title>
				<link>https:/forums/topic/product-stripper-feed-to-fractionator-furnace-flow-control/#post-1351</link>
				<pubDate>Mon, 22 Mar 2021 11:43:29 +0000</pubDate>

									<content:encoded><![CDATA[<p>Dear Mr.Nasser<br />
See the attachments for product stripper pump </p>
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				<guid isPermaLink="false">c13603b7a27f8173f081c3291f06bcc3</guid>
				<title>Abu noor replied to the topic Product stripper feed to fractionator furnace flow control in the forum Process Operations</title>
				<link>https:/forums/topic/product-stripper-feed-to-fractionator-furnace-flow-control/#post-1334</link>
				<pubDate>Sun, 21 Mar 2021 09:17:24 +0000</pubDate>

									<content:encoded><![CDATA[<p>Dear Mr. Nasir<br />
Thanks a lot for your answer.<br />
We have three pumps one turbine driven and others motor dirven.There is no<br />
spillback is provided for this pump.Below is the product stripper level control with 8 passes.</p>
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				<guid isPermaLink="false">e6a110a486598dab63a1e88db06e1fc7</guid>
				<title>Abu noor started the topic Product stripper feed to fractionator furnace flow control in the forum Process Operations</title>
				<link>https:/forums/topic/product-stripper-feed-to-fractionator-furnace-flow-control/</link>
				<pubDate>Fri, 19 Mar 2021 18:29:03 +0000</pubDate>

									<content:encoded><![CDATA[<p>How to control the flow from product stripper feed to fractionator furnace 8 passes after product pumpe started?</p>
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				<guid isPermaLink="false">415d7e2e965955ca3780138e6d7ddac2</guid>
				<title>Abu noor started the topic Conversion in Hydrocraker unit in the forum Hydroprocessing</title>
				<link>https:/forums/topic/conversion-in-hydrocraker-unit/</link>
				<pubDate>Thu, 18 Mar 2021 00:31:29 +0000</pubDate>

									<content:encoded><![CDATA[<p>In our Hydrocraker unit two stages with CLG license and conversion 57%<br />
I want to how much I can get flow rate and volume in each stage roughly for each product.<br />
First stage feed (total feed =285.2m3/hr)<br />
VGO= 212.9 m3/hr<br />
HCGO= 72.3 m3/hr</p>
<p>Treat gas =240279 Nm3/hr</p>
<p>Second stage feed (UCO from Fractionator bottom) = 78.3 m3/hr</p>
<p>Treat gas&hellip;<span class="activity-read-more" id="activity-read-more-452"><a href="https:/forums/topic/conversion-in-hydrocraker-unit/" rel="nofollow ugc">Read more</a></span></p>
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				<guid isPermaLink="false">14327054da726f1fe541d89479c48d48</guid>
				<title>Abu noor started the topic Steam generator level control (3element) in the forum Energy Management</title>
				<link>https:/forums/topic/steam-generator-level-control-3element/</link>
				<pubDate>Fri, 12 Mar 2021 18:08:42 +0000</pubDate>

									<content:encoded><![CDATA[<p>How we can control level in steam generator with three element ?<br />
How the density compensated by level inside steam generator ?<br />
When we can use three elements control?</p>
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				<guid isPermaLink="false">e08f3d63f5525c8998d8b6cf33591d5f</guid>
				<title>Abu noor replied to the topic Catalyst average temperature required after commissioning in the forum Hydroprocessing</title>
				<link>https:/forums/topic/catalyst-average-temperature-required-after-commissioning/#post-1209</link>
				<pubDate>Mon, 01 Mar 2021 09:55:20 +0000</pubDate>

									<content:encoded><![CDATA[<p>If SOR 373 and EOR 404 for reactor inlet and SOR 398 and EOR 409. How much WABT will be initially and when we can increase it based in what?</p>
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				<guid isPermaLink="false">5cb95feef618048b97d8c33775156175</guid>
				<title>Abu noor started the topic Catalyst average temperature required after commissioning in the forum Hydroprocessing</title>
				<link>https:/forums/topic/catalyst-average-temperature-required-after-commissioning/</link>
				<pubDate>Sat, 27 Feb 2021 10:38:47 +0000</pubDate>

									<content:encoded><![CDATA[<p>How much should be catalyst average temperature for Diesel unit and Hydrocraker unit after commissioning?</p>
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				<guid isPermaLink="false">4bf3633c88ceb38116a8fa650f95924b</guid>
				<title>Abu noor replied to the topic Working of Burner Management System of Fired Heater in the forum Energy Management</title>
				<link>https:/forums/topic/fired-heater/?view=all#post-1179</link>
				<pubDate>Mon, 22 Feb 2021 13:15:24 +0000</pubDate>

									<content:encoded><![CDATA[<p>That’s great answer<br />
Thanks a lot </p>
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				<guid isPermaLink="false">a1dcffb6f915368844ade80044260728</guid>
				<title>Abu noor started the topic DHT unit feed filters backwashing frequency increases in the forum Hydroprocessing</title>
				<link>https:/forums/topic/dht-unit-backwashing-frequency-increases/</link>
				<pubDate>Mon, 22 Feb 2021 09:07:52 +0000</pubDate>

									<content:encoded><![CDATA[<p>In our DHT unit back washing increases every 20 -30 minutes per cycle. The feed to this unit are SRGO and LCGO cold and hot. Currently we are facing back pressure and feed controls get fully open and flow is less . What is the issues and how we can solve it?<br />
Thanks</p>
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				<guid isPermaLink="false">7daa2da1bbd3296cc72b0a7bcf1c62e0</guid>
				<title>Abu noor replied to the topic Working of Burner Management System of Fired Heater in the forum Energy Management</title>
				<link>https:/forums/topic/fired-heater/#post-1160</link>
				<pubDate>Sun, 21 Feb 2021 16:29:36 +0000</pubDate>

									<content:encoded><![CDATA[<p>It&#8217;s mentioned in the SOP. The self-regulated main fuel gas valve 160-PCV-0165 is correctly set to the required pressure downstream in the line (0.1kg/cm2g)</p>
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				<title>Abu noor started the topic Hydrocraker unit conversion and product for each stage in the forum Hydroprocessing</title>
				<link>https:/forums/topic/hydrocraker-unit-conversion-and-product-for-each-stage/</link>
				<pubDate>Sun, 21 Feb 2021 16:28:54 +0000</pubDate>

									<content:encoded><![CDATA[<p>In the Hydrocracker unit, the first stage feeds are VGO and HCGO and the second stage feed is UCO from the fractionator bottom. How we can know from the first stage and the second stage we are producing Diesel, Jet A1, light<br />
Naphtha, heavy naphtha, and LPG if total conversion 57%. If there is an excel sheet provided in the answer it will better.</p>
<p>Thanks</p>
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				<title>Abu noor posted an update: In hydrocracker unit if we have feed 215m3/hr to first stage [&#133;]</title>
				<link>https://thepetrosolutions.com/activity/p/399/</link>
				<pubDate>Sun, 21 Feb 2021 15:28:42 +0000</pubDate>

									<content:encoded><![CDATA[<p>In hydrocracker unit if we have feed 215m3/hr to first stage VGO and HCGO and second stage Feed is 65 m3 /hr from fractionator bottom.How we can know how much we produce diesel, Jet A1 , light and heavy naphtha and LPG from both stages and how much conversion for each stage ?if total conversion 57%.if there is excel sheet is provided in the answer&hellip;<span class="activity-read-more" id="activity-read-more-399"><a href="https://thepetrosolutions.com/activity/p/399/" rel="nofollow ugc">Read more</a></span></p>
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				<guid isPermaLink="false">f0b23f94829d185436e39b2199954b65</guid>
				<title>Abu noor started the topic Working of Burner Management System of Fired Heater in the forum Energy Management</title>
				<link>https:/forums/topic/fired-heater/</link>
				<pubDate>Sat, 20 Feb 2021 12:32:52 +0000</pubDate>

									<content:encoded><![CDATA[<p>We have a gas-fired heater with BMS and a globe valve bypass and PCV what’s the purpose of and when we can use it?<br />
How can we control the temperature which is cascaded with fuel gas and how does the logic work?</p>
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