Ph. D. Candidate:Guangming Li Supervisor:Prof. Chul B. Park Study of the Solubility of Gas in a Polymer Melt & Cell Nucleation in Die Microcellular Plastics.

Slides:



Advertisements
Similar presentations
Properties of a Pure Substance
Advertisements

Gas Solubilities Henry’s Law: [A]equilibrium = SA · pA
Extrusion-Based Processes
Melting Temperature Depression of n-Hexadecane Confined in Rubber Networks Qian Qin and Gregory B. McKenna Department of Chemical Engineering, Texas Tech.
Chemical Thermodynamics 2013/ nd Lecture: Zeroth Law, Gases and Equations of State Valentim M B Nunes, UD de Engenharia.
Physical Chemistry I (TKK-2246) 13/14 Semester 2 Instructor: Rama Oktavian Office Hr.: M.13-15, Tu , W , Th.
PETE 310 Lectures # 6 & # 7 Phase Behavior – Pure Substances (Lecture # 5) Two Component Mixtures Three & Multicomponent Mixtures.
Properties of Reservoir Fluids Fugacity and Equilibrium Fall 2010 Shahab Gerami 1.
§ 8.2 Surface phenomenon of liquid Chapter 8 Surface phenomenon and dispersion system.
PETE 310 Lectures # 32 to 34 Cubic Equations of State …Last Lectures.
2. Formation of Cloud droplets
Polymer Synthesis CHEM 421 Polycarbonates: Interfacial Polymerizations Commercially Important Commercially Important Brunelle, D. J. Am. Chem. Soc., 1990,
Solid-vapor equilibrium (SVE) and Solid-liquid equilibrium (SLE)
Interfacial transport So far, we have considered size and motion of particles In above, did not consider formation of particles or transport of matter.
Water.
Applying Gibbs theory on SAFT and PC-SAFT EOS’s to calculate nucleation rates of Ethanol and Methanol. Fawaz Hrahsheh Dr. Abdalla Obeidat Department of.
1 MODELING DT VAPORIZATION AND MELTING IN A DIRECT DRIVE TARGET B. R. Christensen, A. R. Raffray, and M. S. Tillack Mechanical and Aerospace Engineering.
NMR Measurement and Viscosity Evaluation of Live Bitumen Elton Yang, George J. Hirasaki Chemical Engineering Dept. Rice University April 26, 2011.
Chapter 3 Properties of a Pure Substance
Three & Multicomponent Mixtures…
Vapor pressure and liquids Vapor : A gas that exists below its critical point Gas : gas that exists above its critical point ِNote : A gas can not condense.
Study on Supercritical Fluids Thermodynamics Laboratory Dept. of Chemical Eng. National Taiwan University.
Physics A First Course Matter and Energy Chapter 8.
STATES OF MATTER Chemistry CP.
Thermodynamics Basic Review of Byeong-Joo Lee Microstructure Evolution
Numerical Simulation of Physical Foaming Processes
Brookhaven Science Associates U.S. Department of Energy MUTAC Review April , 2004, LBNL Target Simulation Roman Samulyak, in collaboration with.
Distillation ... A Separation Method.
States Of Matter Solids – The particles (atoms) in a solid are packed tightly together and stay in fixed positions. A solid has a definite shape and a.
Material Measurement Laboratory Cryogenic Engineering Conference :45 AM Single-phase ambient and cryogenic temperature heat transfer.
Valves In Industry (Part 3)
PTT 201/4 THERMODYNAMIC SEM 1 (2013/2014). Due to the mixture is not chemically homogeneous Pure substance: A substance that has a fixed chemical composition.
Physical and chemical equilibrium of CO2-Water-Mineral system using Aspen Plus process simulator Technical University of Delft Ali Akbar Eftekhari Hans.
THERMODYNAMICS OF SEPARATION OPERATIONS
Prepared by PhD Halina Falfushynska Lecture 8. Colligative properties of solutions.
High-Pressure Vapor-Liquid and Vapor-Liquid-Liquid Equilibria in the Carbon Dioxide + 1-Nonanol System Catinca Secuianu, Viorel Feroiu, Dan Geană Dept.
Reduced-adiabat Isotherms of Metals and Hard Materials at 100 GPa Pressures and Finite Temperatures W. J. Nellis Department of Physics Harvard University.
Modeling the Adsorption of Mixed-Gases Based on Pure Gas Adsorption Properties Nir Tzabar, Harry J. Holland, Cris H. Vermeer, Marcel H.J. ter Brake Energy,
DALTON’S LAW OF PARTIAL PRESSURE
CHAPTER 13 – States of Matter THE KINETIC THEORY 1.All matter is composed of very small particles 2.These particles are in constant, random motion.
Simple Lattice Model for Fluids. Introduction In this chapter we borrow the idea of lattice structures, characteristic of crystals, and apply it to develop.
Alternative equation for sorption data interpretation Patrick van Hemert & K-H.A.A. Wolf May 25, 2006 International Symposium CBM, Tuscaloosa.
Gas condensate properties. The classical categories of hydrocarbons  Gases  Gas condensates  Volatile oils  Black oils  Heavy oils  Oil sand oils.
Pressure – Volume – Temperature Relationship of Pure Fluids.
Condensed States of Matter: Liquids and Solids Chapter 14
The Study of Structural porosity of melt blown Lyocell fibres
Chapter 5 Single Phase Systems
Chapter 14: Chemical Equilibrium Sections Sarah Rodriguez.
Definitions Polymer Solubility and Thermo $100 $200 $300 $400 $500 Multi- component Materials Polymer Transitions Phase Continuity and Diagrams $400.
Department of Chemical Engineering National Taiwan University Principle Investigator : Yan-Ping Chen Research Group : Min-Long Yu Chyau-Song Wu Jung-Chin.
Chapter 3 PROPERTIES OF PURE SUBSTANCES Dr. Kagan ERYURUK Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.
Aerosol Self Nucleation Why are we interested?  Contribute to natural aerosol concentrations  global warming implications  health implications  serve.
Brookhaven Science Associates U.S. Department of Energy MUTAC Review April , 2004, BNL Target Simulations Roman Samulyak in collaboration with Y.
SOLUTION THERMODYNAMICS:
GASES. Gases  The physical state of gases is defined by several physical properties  Volume  Temperature  Amount (commonly expressed as number of.
Noorulnajwa Diyana Yaacob PPK Bioproses Universiti Malaysia Perlis MULTIPHASE SYSTEM.
Physical Behavior of Matter Review. Matter is classified as a substance or a mixture of substances.
Chapter 14: Phase Equilibria Applications Part II.
Interfacial Tension and Interfacial profiles: The essentials of the microscopic approach Costas Panayiotou University of Thessaloniki, Greece.
© 2010 Borealis AG A Generalized Modelling Tool for the Simulation of Molecular Species Transport and Thermodynamic Properties in Polymer Materials: Applications.
Presented by: Dr. Bader Albusairi Work Done by: Dr. Bader Albusairi Eng. Reem Alkhaldey Chemical Engineering Department College of Engineering and Petroleum.
ASTM D6422 – what’s happening?
PPS AMERICAS CONFERENCE
Gas Properties & PVT Tests
Thermag VII Torino Italy
M. Mahmoodi1, M. Arjmand2, U. Sundararaj2 and S. S. Park1
Determination of dart drop impact resistance for HDPE and LLDPE film grades SL -M 513 Presenter by: Asaf Orujov.
CCE and CVD results The usual PVT measurements on gas condensates are
CCE and CVD results The usual PVT measurements on gas condensates are
Presentation transcript:

Ph. D. Candidate:Guangming Li Supervisor:Prof. Chul B. Park Study of the Solubility of Gas in a Polymer Melt & Cell Nucleation in Die Microcellular Plastics Manufacturing Laboratory, University of Toronto

Outline Introduction Objectives Background Approach Experiments Contributions

Introduction

Plastic Foams Plastic foams Decreased density Cellular structure Advantages over non-foamed plastic Insulating properties Impact resistant characteristics Buoyancy Outstanding strength-to-weight ratios

Plastic Foam Processing Formation of single-phase polymer/gas solution Cell nucleation Cell growth Stabilization Two system + gas polymer Two-phase polymer/gas mixture Single- phase polymer/gas solution Gas injectionMixing & diffusion Diffusion

Plastic Foam Processing Formation of single-phase polymer/gas solution Cell nucleation Cell growth Stabilization Distance P solubility Die Pressure

Objectives

To systematically investigate the gas solubility for different polymer/gas mixture systems To verify the solubility pressure inside the die during the continuous plastic foaming process

Background

Pressure Decay + SL-EOS Y. Sato, etc., Fluid Phase Equilibria 162 (1999) 261; for N 2 and CO 2 in PP, HDPE and PS Electrobalance + Partial Volume by Henrian Sorption Theory B. Wong, etc., Journal of Polymer Science (Part B) 36 (1998) 2025; for PS + CO 2 and PVC + CO 2 Previous Study of Solubility

Application of Gas Solubility in an Extrusion Die PRESSURE VOLUME Isotherm Critical Point Saturated Vapor (Binodal) Liquid Spinodal Vapor Spinodal Saturated Liquid

The minimum work to create a bubble (radius R) The bubble nucleation rate

Approach

Theoretical Prediction of Gas Solubility The fundamental concept of this approach is that the chemical potential of a vapor is equal to the chemical potential of its condensate in the polymer melt, when the equilibrium condition is reached. A(G) A(P) +B(P) Equal at equilibrium A: Gas B: Polymer G: Gas phase P : Polymer/Gas Solution phase

Segment of Component A Segment of Component B Empty cell (hole) Equation-of-State for the Multi-component System (Gas/Polymer Mixture) Lattice-Fluid Model (Sanchez and Lacombe EOS) Hole Model (Simha and Somcynsky EOS)

SL Model

SS Model

(High pressure gas) Buoyancy Compensation + ) Volume of Swelling Solubility F(P,T)- F(0,T)+ ρ gas × ( + Volume of holder Initial Volume of pure polymer at P,T Apparent Solubility F is Balance Reading (Vacuum) F(0,T) microbalance Polymer Sample microbalance F(P,T) Experimental Measurement of the Solubility by MSB

Volume of Swelling Swollen volume contributed buoyancy effect is an outstanding factor on solubility measurement in high pressure conditions. Theoretical method ( Equation-of-State) to predict the swollen volume.

Theoretical Estimation of Volume of Swelling SL EOS: SS EOS:

Actual Measurement of Volume of Swelling -Pendent Droplet Method Pendent drop in high temperature and pressure cell is currently utilized to do the PVT density measurement by examining the final volume after swelling. Polymer droplet High T and P cell Scale Rod gas

Experiments

Comparison of SL EOS and SS EOS Polystyrene (PS, T g =381.4K, M w =3.30×10 5, M n = 1.07×10 5 ), A&M Styrene Corporation, (Kawasaki, Japan). Carbon dioxide (Coleman grade, 99.99% purity), BOC Canada. Materials: Equipment: MSB

a b c d e f a: Microbalance b: Measuring cell c: Temperature control device d: Gas dosing system e: Control panel f: Data acquisition system Schematic of MSB Instrument MSB

Proposed Procedure to Determine the Solubility Obtain set of Apparent Solubility (AS) experimentally. Set an initial value of EOSs interaction parameter(s). Calculate the difference of the corrected solubility and theoretical solubility:  (CS i - S i ) 2 Obtain the corresponding set of the Theoretical Solubility (S) and the density of polymer/gas mixture based on SS or SL EOS. Obtain the Corrected Solubility (CS) using the SS-based or SL- based swollen volume. Decide the optimum interaction parameter(s) by minimizing  (CS i - S i ) 2

Volume Swelling effect prediction (a)SS-based and SL-based prediction at 110 o C; (b)SS-based and SL-based prediction at 150 o C; (c)SS-based and SL-based prediction at 200 o C; (b)(a)(a) (c)(c)

Solubility of CO 2 in Polystyrene at C

Solubility of CO 2 in Polystyrene at C

Solubility of CO 2 in Polystyrene at C

Temperature Effect on Interaction Parameters of EOS K 12 of SL-EOSδ e and δ v of SS-EOS δ e = δ v =

Sub-conclusion SL EOS and SS EOS predicted different swollen volumes. Below 1500 psi, corrected solubilities from SL and SS EOS are very close to each other. Above 1500 psi, there are significant difference between the SL EOS and SS EOS in terms of the solubility measurement. The interaction parameters for SL EOS and SS EOS show different temperature dependence.

Investigation of the Solubility of CO 2 in Branched –PP and Linear-PP

Rheological Behavior Difference Between the Branched-PP and Linear PP This behavior of LCB-PP is beneficial to all the processes involving extensional flow, such as thermoforming, foaming and blow molding Branched-PP Linear-PP Branched-PP

5% CO 2 content SL-EOS SS-EOS 10% CO 2 content

Solubility for linear PP/CO 2 mixture and branched PP/CO2 by SL EOS

Solubility for linear PP/CO 2 mixture and branched PP/CO2 by SS EOS

Investigation of the Solubility of CO 2 in Polycarbonate and the Effect of Crystallinity on Solubility Tough Transparent Crystallizable (regular chemical structure) Extremely low crystallization rate (chain rigidity) Material

Uptake curve for the sorption of CO 2 in PC 160 o C 200 o C240 o C

Investigation of the Crystallization of PC induced by CO 2 at 160 o C Original PC PC treated with CO 2 at 160 o C for 24 hrs (crystallinity is 21.66%) Polarizing Light Microscope DSC

Solubility of CO 2 in PC at 200 o C and 240 o C 240 o C 200 o C

System Design for Study of Solubility Pressure inside the Die

Upgrade the primary 1.5" extruder with 30:1 L/D ratio. Upgrade gear pump (Zenith, PEP-II 10 cc/rev) for controlling the melt flow rate up to 100 g/min. Secondary 1.5" extruder with a mixing screw of 24:1 L/D ratio attached after the gear pump. Die design

Contributions

Development of experimental approach to study the solubility of gas in a polymer at elevated temperature and pressure; Development of a theoretical approach to predict the swollen volume for the polymer/gas mixture; Investigation of the solubility of various gases in different polymer melts; Solubility Study Nucleation investigation The investigation on the nucleation inside the die theory.

Research Timetable Please see the attached Report

Thank You!