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No chemical process facility is immune to the risk of overpressure to avoid dictating the necessity for overpressure protection. For every situation that demands safe containment of process gas, it becomes an obligation for engineers to equally provide pressure relieving and flaring provisions wherever necessary. The levels of protection are hierarchical, starting with designing an inherently safe process to avoid overpressure followed by providing alarms for operators to intervene and Emergency Shutdown provisions through ESD and SIL rated instrumentation. Beyond these design and instrument based protection measures, the philosophy of containment and abatement steps such as pressure relieving devices, flares, physical dikes and Emergency Response Services is employed
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Centrifugal Compressors are a preferred choice in gas transportation industry, mainly due to their ability to cater to varying loads. In the event of a compressor shutdown as a planned event, i.e., normal shutdown (NSD), the anti-surge valve is opened to recycle gas from the discharge back to the suction (thereby moving the operating point away from the surge line) and the compressor is tripped via the driver (electric motor or Gas turbine / Steam Turbine). In the case of an unplanned event, i.e., emergency shutdown such as power failure, the compressor trips first followed by the anti-surge valve opening. In doing so, the gas content in the suction side & discharge side mix. Therefore, settle out conditions is explained as the equilibrium pressure and temperature reached in the compressor piping and equipment volume following a compressor shutdown
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This is course on Plant Simulation will show you how to setup hypothetical compounds, oil assays, blends, and petroleum characterization using the Oil Manager of Aspen HYSYS. You will learn about: Hypothetical Compounds (Hypos) Estimation of hypo compound data Models via Chemical Structure UNIFAC Component Builder Basis conversion/cloning of existing components Input of Petroleum Assay and Crude Oils Typical Bulk Properties (Molar Weight, Density, Viscosity) Distillation curves such as TBP (Total Boiling Point) ASTM (D86, D1160, D86-D1160, D2887) Chromatography Light End Oil Characterization Using the Petroleum Assay Manager or the Oil Manager Importing Assays: Existing Database Creating Assays: Manually / Model Cutting: Pseudocomponent generation Blending of crude oils Installing oils into Aspen HYSYS flowsheets Getting Results (Plots, Graphs, Tables) Property and Composition Tables Distribution Plot (Off Gas, Light Short Run, Naphtha, Kerosene, Light Diesel, Heavy Diesel, Gasoil, Residue) Oil Properties Proper Boiling Point Curves Viscosity, Density, Molecular Weight Curves This is helpful for students, teachers, engineers and researchers in the area of R&D, specially those in the Oil and Gas or Petroleum Refining industry. This is a "workshop-based" course, there is about 25% theory and about 75% work! At the end of the course you will be able to handle crude oils for your fractionation, refining, petrochemical process simulations!
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We are all familiar with the production systems through which reservoir fluids flow to reach our processing facilities. This is a journey characterized by complex multiphase flow phenomena that govern pressure and temperature changes along the way. A monumental amount of research and development work has been invested towards better understanding multiphase flow behavior over the past fifty years. Yet, many challenges remain as we strive to optimize ever more complex production systems fraught with difficult flow assurance issues. Just how good is the science? And more importantly, how does this impact our bottom line? This lecture will discuss key concepts of multiphase flow leading to the current “state-of-the-art” models used today. Looking towards the future, the science must be advanced to address areas of greatest uncertainty and align with trends in field development strategies. Recommendations will be presented covering the top 5 areas of research necessary for these purposes. The economic impact of multiphase operations will be illustrated using two examples that provide insight towards maximizing asset value. Mack Shippen is a Principal Engineer with Schlumberger in Houston, where he is responsible for the global business of the PIPESIM multiphase flow simulation software. He has extensive experience in well and network simulation studies, ranging from flow assurance to dynamic coupling of reservoir and surface simulation models. He has served on a number of SPE committees and chaired the SPE Reprint Series on Offshore Multiphase Production Operations. He holds BS and MS degrees in Petroleum Engineering from Texas A&M University, where his research focused on multiphase flow modelling.
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Society of Petroleum Engineers
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This presentation covers materia
Material & Energy Balance for Distillation
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Pankaj Khandelwal
No chemical process facility is immune to the risk of overpressure to avoid dictating the necessity for overpressure protection. For every situation that demands safe containment of process gas, it becomes an obligation for engineers to equally provide pressure relieving and flaring provisions wherever necessary. The levels of protection are hierarchical, starting with designing an inherently safe process to avoid overpressure followed by providing alarms for operators to intervene and Emergency Shutdown provisions through ESD and SIL rated instrumentation. Beyond these design and instrument based protection measures, the philosophy of containment and abatement steps such as pressure relieving devices, flares, physical dikes and Emergency Response Services is employed
Pressure Safety Valve Sizing - API 520/521/526
Pressure Safety Valve Sizing - API 520/521/526
Vijay Sarathy
Centrifugal Compressors are a preferred choice in gas transportation industry, mainly due to their ability to cater to varying loads. In the event of a compressor shutdown as a planned event, i.e., normal shutdown (NSD), the anti-surge valve is opened to recycle gas from the discharge back to the suction (thereby moving the operating point away from the surge line) and the compressor is tripped via the driver (electric motor or Gas turbine / Steam Turbine). In the case of an unplanned event, i.e., emergency shutdown such as power failure, the compressor trips first followed by the anti-surge valve opening. In doing so, the gas content in the suction side & discharge side mix. Therefore, settle out conditions is explained as the equilibrium pressure and temperature reached in the compressor piping and equipment volume following a compressor shutdown
CENTRIFUGAL COMPRESSOR SETTLE OUT CONDITIONS TUTORIAL
CENTRIFUGAL COMPRESSOR SETTLE OUT CONDITIONS TUTORIAL
Vijay Sarathy
This presentation file provides a quick refresher to pressure relief valve sizing for single phase flow. The calculation guideline is as per API Std 520.
Pressure Relief Valve Sizing for Single Phase Flow
Pressure Relief Valve Sizing for Single Phase Flow
Vikram Sharma
This is course on Plant Simulation will show you how to setup hypothetical compounds, oil assays, blends, and petroleum characterization using the Oil Manager of Aspen HYSYS. You will learn about: Hypothetical Compounds (Hypos) Estimation of hypo compound data Models via Chemical Structure UNIFAC Component Builder Basis conversion/cloning of existing components Input of Petroleum Assay and Crude Oils Typical Bulk Properties (Molar Weight, Density, Viscosity) Distillation curves such as TBP (Total Boiling Point) ASTM (D86, D1160, D86-D1160, D2887) Chromatography Light End Oil Characterization Using the Petroleum Assay Manager or the Oil Manager Importing Assays: Existing Database Creating Assays: Manually / Model Cutting: Pseudocomponent generation Blending of crude oils Installing oils into Aspen HYSYS flowsheets Getting Results (Plots, Graphs, Tables) Property and Composition Tables Distribution Plot (Off Gas, Light Short Run, Naphtha, Kerosene, Light Diesel, Heavy Diesel, Gasoil, Residue) Oil Properties Proper Boiling Point Curves Viscosity, Density, Molecular Weight Curves This is helpful for students, teachers, engineers and researchers in the area of R&D, specially those in the Oil and Gas or Petroleum Refining industry. This is a "workshop-based" course, there is about 25% theory and about 75% work! At the end of the course you will be able to handle crude oils for your fractionation, refining, petrochemical process simulations!
Aspen HYSYS - Petroleum Assays and Oil Characterization (Slideshare)
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Chemical Engineering Guy
We are all familiar with the production systems through which reservoir fluids flow to reach our processing facilities. This is a journey characterized by complex multiphase flow phenomena that govern pressure and temperature changes along the way. A monumental amount of research and development work has been invested towards better understanding multiphase flow behavior over the past fifty years. Yet, many challenges remain as we strive to optimize ever more complex production systems fraught with difficult flow assurance issues. Just how good is the science? And more importantly, how does this impact our bottom line? This lecture will discuss key concepts of multiphase flow leading to the current “state-of-the-art” models used today. Looking towards the future, the science must be advanced to address areas of greatest uncertainty and align with trends in field development strategies. Recommendations will be presented covering the top 5 areas of research necessary for these purposes. The economic impact of multiphase operations will be illustrated using two examples that provide insight towards maximizing asset value. Mack Shippen is a Principal Engineer with Schlumberger in Houston, where he is responsible for the global business of the PIPESIM multiphase flow simulation software. He has extensive experience in well and network simulation studies, ranging from flow assurance to dynamic coupling of reservoir and surface simulation models. He has served on a number of SPE committees and chaired the SPE Reprint Series on Offshore Multiphase Production Operations. He holds BS and MS degrees in Petroleum Engineering from Texas A&M University, where his research focused on multiphase flow modelling.
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Gerard B. Hawkins
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tanu pandey
Welcome to the April edition of WIPAC Monthly, the magazine brought to you by Water Industry Process Automation & Control. In this month's edition, along with the latest news from the industry we have articles on: The use of artificial intelligence and self-service platforms to improve water sustainability A feature article on measuring wastewater spills An article on the National Underground Asset Register Have a good month, Oliver
Water Industry Process Automation & Control Monthly - April 2024
Water Industry Process Automation & Control Monthly - April 2024
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Gerard B. Hawkins
Versión en Ingles de manual del ingeniero químico, 7ma edición. Capitulo 14
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KAMALESH KUMAR
Excel sheet Download Link: https://www.scribd.com/document/385945712/PSV-Sizing-Tool-API-Based-Calc-Sheets PSV Sizing for Blocked Liquid Discharge Condition PSV Sizing for Blocked Gas Discharge Condition PSV Sizing for Fire Case of Liquid Filled Vessel PSV Sizing for Control Valve Fail Open Case Relief Valve Sizing for Thermal Expansion Restriction Orifice Sizing for Gas Flow Restriction Orifice Sizing for Liquid Flow Single Phase Flow Line Sizing Tool Gas Control Valve Sizing Tool
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The explosion hazard in urea process (1)
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Was ist angesagt?
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flare system design.pdf
flare system design.pdf
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Antoine coefficient table
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Bhosari ( Call Girls ) Pune 6297143586 Hot Model With Sexy Bhabi Ready For ...
Bhosari ( Call Girls ) Pune 6297143586 Hot Model With Sexy Bhabi Ready For ...
tanu pandey
Welcome to the April edition of WIPAC Monthly, the magazine brought to you by Water Industry Process Automation & Control. In this month's edition, along with the latest news from the industry we have articles on: The use of artificial intelligence and self-service platforms to improve water sustainability A feature article on measuring wastewater spills An article on the National Underground Asset Register Have a good month, Oliver
Water Industry Process Automation & Control Monthly - April 2024
Water Industry Process Automation & Control Monthly - April 2024
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AKTU Computer Networks notes --- Unit 3.pdf
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Thermal Engineering Unit - I & II . ppt
Thermal Engineering Unit - I & II . ppt
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Double field revolving theory: According to the double field revolving theory, we can resolve any alternating quantity into two components. Each component has a magnitude equal to half of the maximum magnitude of the alternating quantity, and both these components rotate in the opposite direction to each other
Double Revolving field theory-how the rotor develops torque
Double Revolving field theory-how the rotor develops torque
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University management System project report..pdf
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FEA Based Level 3 Assessment of Deformed Tanks with Fluid Induced Loads
FEA Based Level 3 Assessment of Deformed Tanks with Fluid Induced Loads
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Rule 1 − Check for the blocks connected in series and simplify. Rule 2 − Check for the blocks connected in parallel and simplify. Rule 3 − Check for the blocks connected in feedback loop and simplify. Rule 4 − If there is difficulty with take-off point while simplifying, shift it towards right. Rule 5 − If there is difficulty with summing point while simplifying, shift it towards left. Rule 6 − Repeat the above steps till you get the simplified form, i.e., single block.
Block diagram reduction techniques in control systems.ppt
Block diagram reduction techniques in control systems.ppt
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Unit 2- Effective stress & Permeability.pdf
Unit 2- Effective stress & Permeability.pdf
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AKTU Computer Networks notes --- Unit 3.pdf
AKTU Computer Networks notes --- Unit 3.pdf
Thermal Engineering Unit - I & II . ppt
Thermal Engineering Unit - I & II . ppt
Double Revolving field theory-how the rotor develops torque
Double Revolving field theory-how the rotor develops torque
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University management System project report..pdf
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Block diagram reduction techniques in control systems.ppt
Block diagram reduction techniques in control systems.ppt
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