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Optimal Process Design of 2- and 3-Phase Horizontal Production Separators for Oil and Gas Installations: A Mathematical Programming Formulation in Excel 2016

Optimal Process Design of 2- and 3-Phase Horizontal Production Separators for Oil and Gas Installations: A Mathematical Programming Formulation in Excel 2016

Optimal Process Design of 2- and 3-Phase Horizontal Production Separators for
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Optimal Process Design of 2- and 3-Phase Horizontal Production Separators for Oil and Gas Installations: A Mathematical Programming Formulation in Excel 2016 Paperback - 2019

by John T Small

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  • Title Optimal Process Design of 2- and 3-Phase Horizontal Production Separators for Oil and Gas Installations: A Mathematical Programming Formulation in Excel 2016
  • Author John T Small
  • Binding Paperback
  • Condition New
  • Pages 80
  • Volumes 1
  • Language ENG
  • Publisher Independently Published
  • Publication date 2019-09-22
  • Bookseller's Inventory # 38840598
  • ISBN 9781694977212 / 1694977218
  • Weight 0.61 lbs (0.28 kg)
  • Dimensions 11 x 8.5 x 0.21 in (27.94 x 21.59 x 0.53 cm)
  • Category Technology & Industrial Arts
  • Quantity available 5

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Reader reviews for Optimal Process Design of 2- and 3-Phase Horizontal Production Separators for Oil and Gas Installations: A Mathematical Programming Formulation in Excel 2016

From the publisher

This book details a Microsoft Excel spreadsheet which models numerically the following key design factors for horizontal separators and optimizes the vessel dimensions using the Solver add-in, allowing the engineer to minimize the size of the vessel and associated piping whilst achieving satisfactory performance in the separation, process control and safeguarding functions: -Gravity settling zone dimensions for successful phase separation. -Provision of adequate liquid hold up times and height differences between contiguous level control and trip settings.-Type of inlet device, and its impact upon the size of inlet pipework and the dimensions of the separator vessel.-Nozzle sizing according to erosional, velocity head and velocity criteria, and the impact on vessel dimensions.-Maintaining axial velocities of oil and water phases within acceptable limits.-Prevention of re-entrainment of oil droplets into the gas phase.-Prevention of transient gas blowby or gross carryover of liquid during unplanned shutdown.-Provision of adequate liquid and gas holdup volumes for slugging and surging.-Prevention of spurious trips due to foaming, where applicable.The principal calculation method for dimensioning the gravity settling zone of the vessel is based on settling theory, according to which droplets / bubbles of certain diameters settle to their respective continuous phases, however the spreadsheet allows the engineer to concurrently specify minimum allowable oil and / or water retention times if desired.
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