Depressuring Flow - Quick Manual Method

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Chemical & Process Technology A place to share knowledge, lesson learnt... HOME ARCHIVE LINK FREE MAGAZINES FOLLOW ME Enter your email address: SUPPORT This Site Hot Posts FREE Info Free Newsletter Free Magazine Latest Posts Crevice Corrosion Engineering Guide Software for S... Role of CE in BioTech Talk FREE KG-TOWER V4 Crevice Corrosion Mechanism & Prevention Stainless Steel and It Selection Training Module FREE Chemical Engineering Digital Issue for Jan 20... Determine Corrosion Allownace (CA) with Corrosion ... LNG SES Issues... Additional Concerns in Controlled Depressuring Some Comments on Thermal Expansion... Links Chem & Proc tech Oil & Gas tech Heat Exch tech Gen Tech Webworm DC Chemical and Process Engineering Chemical Engineering World Smart Process Design ChEng Visitors Web Chem & Proc Tech CHEM & PROC TECH OIL & GAS TECH HEAT & EXCH TECH GEN TECH Depressuring Flow - Quick Manual Method Sunday, January 25, 2009 Display problem ? Click HERE Recommended : Subscribe FREE - Processing Magazine Depressuring system is provided in Oil and gas, Gas & LNG plant, etc to evacuate the inventory from process system as fast as possible so that the reduced internal pressure stresses is kept below the rupture stress. This has been discussed in "Depressuring within 15 minutes no longer applicable ?". Nevertheless, quick depressuring may lead to other problem such as low temperature embrittlement, excessive noise and vibration, etc. Depressure a high pressure would lead to low temperature of depressured system and failure due to low temperature embrittlement. Higher the depressuring rate, lower the temperature can be experienced by depressured system. Thus, the restriction orifice (RO) downstream of Blowdown Valve (BDV) in depressuring system primarily is to limit flow so that the temperature will not drop below the allowable lowest temperature limit of material. This has been discussed in "Don't misunderstood depressuring". Although depressuring shall be implemented within the shortest time possible, excessive depressuring may potentially lead to damage to equipment such as compressor seal, solid bed, etc. Thus, there are two type of depressuring as discussed in "Controlled and Non-controlled Type Depressuring". Nevertheless, it is emphasized again here, depressuring system shall be designed to bring plant to safe level without any tolerance. Many depressuring systems are designed to depressure the system within 15 minutes follow recommendation in API 521. Nevertheless, one shall take note that the 15 minutes is sort of arbitrary and may be good for some system and configuration. Thus, in most recent API STD 521, the requirement has slightly changed where a depressuring system shall be designed such that the stress induced by internal pressure of a system is lower than stress allowable by the system. This may lead to shorter depressuring time as discussed in "Depressuring within 15 minutes no longer applicable ?". Recommended : Subscribe FREE -Pipeline & Gas Technology Depressuring can be conducted using simple depressuring module in process simulator such HYSYS, PRO-II, etc. One shall understood there are limitation and accuracy issue in above mentioned depressuring modules and shall be used with care. There are other depressuring simulator such as LNGDYN by TECHNIP, BLOWDOWN by Imperial College, etc which are calculated rigorously and tested with real plant data. It is always advisable to use these simulator for specific case. Assumption In this post, a manual depressuring method is introduced. This method is first introduced by Grote and are derived base on following assumptions : i) Critical flow throughout entire depressuring process ii) Constant mass flow throughout entire depressuring process iii) System being depressured is maintained as gaseous throughout entire depressuring process iv) Constant temperature, molecular weight and compressibility Methodology Following is the derivation of the manual equation. How to apply valve equation in HYSYS Depressuring ? High pressure and moderate/low temperature operation are common in oil and gas industry. High pressure system with large vessels will lead to large inventory and it significantly increases hazardous level to personnel and assets... Chemical & Process Technology: Depressuring Flow - Quick Manual M... http://webwormcpt.blogspot.com/2009/01/depressuring-quick-manual-m... 1 of 3 15/06/2015 23:48

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BDVQuick Manual Method

Transcript of Depressuring Flow - Quick Manual Method

  • Chemical & Process TechnologyA place to share knowledge, lesson learnt...

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    Depressuring Flow - Quick Manual MethodSunday, January 25, 2009

    Display problem ? Click HERE

    Recommended :Subscribe FREE - Processing Magazine

    Depressuring system is provided in Oil and gas, Gas & LNG plant,etc to evacuate the inventory from process system as fast aspossible so that the reduced internal pressure stresses is keptbelow the rupture stress. This has been discussed in"Depressuring within 15 minutes no longer applicable ?".Nevertheless, quick depressuring may lead to other problem suchas low temperature embrittlement, excessive noise andvibration, etc. Depressure a high pressure would lead to lowtemperature of depressured system and failure due to lowtemperature embrittlement. Higher the depressuring rate, lower thetemperature can be experienced by depressured system. Thus, therestriction orifice (RO) downstream of Blowdown Valve (BDV) in

    depressuring system primarily is to limit flow so that the temperature will not drop belowthe allowable lowest temperature limit of material. This has been discussed in "Don'tmisunderstood depressuring".

    Although depressuring shall be implemented within the shortest time possible, excessivedepressuring may potentially lead to damage to equipment such as compressor seal, solidbed, etc. Thus, there are two type of depressuring as discussed in "Controlled andNon-controlled Type Depressuring". Nevertheless, it is emphasized again here,depressuring system shall be designed to bring plant to safe level without any tolerance.

    Many depressuring systems are designed to depressure the system within 15 minutesfollow recommendation in API 521. Nevertheless, one shall take note that the 15 minutesis sort of arbitrary and may be good for some system and configuration. Thus, in mostrecent API STD 521, the requirement has slightly changed where a depressuring systemshall be designed such that the stress induced by internal pressure of a system is lowerthan stress allowable by the system. This may lead to shorter depressuring time asdiscussed in "Depressuring within 15 minutes no longer applicable ?".

    Recommended :Subscribe FREE -Pipeline & Gas Technology

    Depressuring can be conducted using simple depressuringmodule in process simulator such HYSYS, PRO-II, etc. One shallunderstood there are limitation and accuracy issue in abovementioned depressuring modules and shall be used with care.There are other depressuring simulator such as LNGDYN byTECHNIP, BLOWDOWN by Imperial College, etc which arecalculated rigorously and tested with real plant data. It is alwaysadvisable to use these simulator for specific case.

    AssumptionIn this post, a manual depressuring method is introduced. Thismethod is first introduced by Grote and are derived base onfollowing assumptions :

    i) Critical flow throughout entire depressuring processii) Constant mass flow throughout entire depressuring processiii) System being depressured is maintained as gaseous throughout entire depressuringprocessiv) Constant temperature, molecular weight and compressibility

    MethodologyFollowing is the derivation of the manual equation.

    How to apply valve equation in HYSYSDepressuring ?High pressure and moderate/low temperature operationare common in oil and gas industry. High pressuresystem with large vessels will lead to large inventoryand it significantly increases hazardous level topersonnel and assets...

    Chemical & Process Technology: Depressuring Flow - Quick Manual M... http://webwormcpt.blogspot.com/2009/01/depressuring-quick-manual-m...

    1 of 3 15/06/2015 23:48

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    August 2012Concluding RemarkEquation [5] may be used for manual depressuring if a system inventory (initial mass, M0),depressuring time (t), initial (P0) and final pressure (P) are are known. One shall check theassumptions are valid before it is used. This equation may be used as quick method to

    Chemical & Process Technology: Depressuring Flow - Quick Manual M... http://webwormcpt.blogspot.com/2009/01/depressuring-quick-manual-m...

    2 of 3 15/06/2015 23:48

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    determine the depressuring flowrate for quick estimate, however it is not recommendedduring detailed design.

    Related PostAdditional Concerns in Controlled DepressuringDepressuring - Save Some Time in HYSYS - FLARENET IterationFew Recommendation on Manual Blowdown LineA refresh to Process Engineer on few phenomenons in restriction orificeBug in ASPENTECH HYSYS 2006 Dynamic Depressuring Fisher Valve modelHow to apply valve equation in HYSYS Depressuring ?Why Restriction Orifice is some distance from Blowdown valve ?

    Labels: Depressurization, HYSYS

    posted by Webworm, 4:41 PM

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