'Bubble point' diaporamas de présentation

BIOMAN 2011 CHO- tPA Production System Downstream Processing

BIOMAN 2011 CHO- tPA Production System Downstream Processing. Mike Fino MiraCosta College. Unit Operations. Many decisions to be made at each step in the process. Downstream Example. Harvest Separation (Clarification).

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Cryogenic Fluid Management Technology for Exploration

Cryogenic Fluid Management Technology for Exploration. DLT Forum Presentation April 7, 2006 RTP/Propellant Systems Branch Maureen Kudlac Neil Van Dresar Dave Plachta. Recent CFM Funding Chronology. FY04. FY05. FY06. FY07. FY08. FY. Next Generation Launch Technology Program (NGLT)

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Solution Thermodynamic:

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A Seminar On Validation Of Membrane Filtration

A Seminar On Validation Of Membrane Filtration. Quality Assurance Department Maliba Pharmacy College. Content. Introduction Objectives Why validation needed Pre-requisites for validation Validation Study Element References. Introduction.

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PETE 310 Lectures # 25 -26

PETE 310 Lectures # 25 -26. Chapter 12 Gas-Liquid Equilibrium. Gas-Liquid Equilibrium Ideal Behavior. Applications to low pressures Simplifications the gas phase behaves as an Ideal Gas the liquid phase exhibits Ideal Solution Behavior. Ideal Behavior.

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Principales Aportaciones del Dr. Ismael Herrera Revilla a la Industria Petrolera

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Principales Aportaciones del Dr. Ismael Herrera Revilla a la Industria Petrolera

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Chapter 6. Multiphase Systems

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Chapter 6. Multiphase Systems

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CHE 205

CHE 205. Energy Balances. Vapor/Liquid Equilibrium. Multiphase Systems. Nonreactive Processes. $200. $200. $200. $200. $400. $400. $400. $400. $600. $600. $600. $600. $800. $800. $800. $800. $1000. $1000. $1000. $1000.

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PETE 310

PETE 310. Lecture # 26 Chapter 12 Gas-Liquid Equilibrium Non-ideal VLE. Gas-Liquid Equilibrium Non Ideal Behavior. Applications to low & high pressures Use models for the equilibrium ratios (ki-values) Simpler models ki = f (P,T) More complex models ki = f(P,T,compositions)

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PRESSURE PULSE ANALYSIS OF GAS LIFT WELLS

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VLE Calculations

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Problems on Flash Calculations using both Aspen Plus and PRO/II

Problems on Flash Calculations using both Aspen Plus and PRO/II. ? ? ? Ph.D. 4 th week 9/10, 2001 through 9/14, 2001. Ex-1 : Isothermal Flash Calculation. A liquid mixture consisting of 60 mole% benzene, 40 mole% toluene is flashed at 1.2 atm and 100 o C.

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P,T-Flash Calculations

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