Nucleation and growth kinetics and the density of C-S-H. -Shashank Bishnoi & Karen L. Scrivener

Similar documents
MODELLING AUTOGENOUS SHRINKAGE OF HYDRATING CEMENT PASTE

Slurry concentration [Vol.%]

Chapter 10, Phase Transformations

Kinetics. Rate of change in response to thermodynamic forces

CHAPTER 5: DIFFUSION IN SOLIDS

- paste cement-water mix allowing setting and hardening to occur w/c: setting stiffening without significant increase in strength

MACRO- AND MICROSTRUCTURES

Phase field simulations for grain growth in materials containing second-phase particles

POZZOLANIC REACTIVITY OF GROUND GRANULATED BLAST FURNACE SLAG IN BLENDED CEMENT

Part III : Nucleation and growth. Module 4 : Growth of precipitates and kinetics of nucleation and growth. 4.1 Motivating question/phenomenon

STUDIES ON SMALL IONIC DIFFUSIVITY CONCRETE

Mathematical Model of RuO 2 /Carbon Composite Electrode for Supercapacitors

DETERMINATION OF AVRAMI PARAMETER IN THE CASE OF NON-ISOTHERMAL SURFACE CRYSTALLIZATION OF POWDERED GLASSES

EFFECT OF BOTH TALC FINENESS AND TALC LOADING ON HETEROGENEOUS NUCLEATION OF BLOCK COPOLYMER POLYPROPYLENE

CHAPTER SEVEN EXPERIMENTAL RESULTS EFFECT OF THE STEEL S COMPOSITION 7.1 EFFECT OF ANNEALING TREATMENT ON STEEL B

Cooling and hardening during injection molding of field joint coatings for deep sea pipelines

GLASS CULLET AS A NEW SUPPLEMENTARY CEMENTITIOUS MATERIAL (SCM) MOHAMMADREZA MIRZAHOSSEINI

Multi-scale simulation of capillary pores and gel pores in Portland cement paste

Binary Phase Diagrams - II

Atmospheric Ice Nucleation

Diffusional Transformations in Solids

Accumulation (%) Amount (%) Particle Size 0.1

Models for the Yield Strength of Al-Zn-Mg-Cu Alloys

Module 32. Heat treatment of steel II. Lecture 32. Heat treatment of steel II

EFFECTS OF POZZOLANIC REACTION ON THE EVOLUTION OF COARSE CAPILLARY PORE STRUCTURE AND PHASE CONSTITUTION IN CEMENT PASTES WITH MINERAL ADMIXTURES

Age Strengthening of Gray Iron Kinetics Study

Modelling the Effect of Room Temperature Storage and Deformation on the Age-hardening Behaviour of Al-Mg-Si alloys

Assessment of Nucleation Kinetic Mechanisms in Gas Hydrate Crystallization Processes

Experimental O 3. Results and discussion

A New Approach to Modeling the Nucleation and Growth Kinetics of Tricalcium Silicate Hydration

Chapter 4. Ionic conductivity of GDC. electrolyte

Optimization of porous current collectors for PEM water electrolysers

Introduction to Heat Treatment. Introduction

8. Principles of Solidification

Corrosion Rates. OLI model basics Polarization curves

Phase Transformations Workshop David Laughlin

Part II : Interfaces Module 3 : Nucleation of precipitates from a supersaturated matrix

Influence of Tertiary Alkanolamines on the Hydration of Portland Cement. Josephine Cheung

Kinetics of austenite formation during continuous heating in a low carbon steel

Keywords. Aluminium-based amorphous alloys; melt spinning; crystallization behaviour; microhardness.

Chemical Engineering 160/260 Polymer Science and Engineering. Lecture 17: Kinetics and Thermodynamics of Crystallization February 26, 2001

A Novel Physics Node for Nakamura Crystallization Kinetics


27-302, Microstructure & Properties II, A.D. Rollett. Fall Homework 2, due Weds, Nov. 6 th

Chapter 10: Phase Transformations

The Effect of Supercooling on the Properties of Thin Saline Ice Layers

Lessons learned while watching paint dry: film formation, drying fronts, and cracking

Chapter 10: Phase Transformations

A COUPLED TRANSPORT-REACTION MODEL FOR SIMULATING AUTOGENOUS SELF-HEALING IN CEMENTITIOUS MATERIALS PART II: VALIDATION

THE INFLUENCE OF TRIETANOLAMINE (TEA) ON CHARACTERISTICS OF FRESH AND HARDENED MORTARS CONTAINING LIMESTONE POWDER

Chapter 3: Powders Production and Characterization

CHAPTER 4: The wetting behaviour and reaction of the diamond-si system

Assoc.Prof.BOONCHAI STITMANNAITHUM. Department of Civil Engineering, Faculty of Engineering Chulalongkorn University, Thailand

Effect of Grain Size Distribution on Elastic Velocity

Novel Wide-Pore Superficially Porous Particles for Biomacromolecular Separations

Deep Sea Hydrate Flow Assurance Challenges

Chapter 10: Phase Transformations

EVALUATION OF THERMAL FATIGUE PROPERTIES OF HSS ROLL MATERIALS. Jong Il Park a Chang Kyu Kim b Sunghak Lee b

LECTURE NO. 7 & 8 SETTING OF CEMENT AND MICROSTRUCTURE OF HYDRATED CEMENT PASTE

The Effects of Dispersoids on the Recrystallization Behavior in a Cold Rolled AA3103-Aluminium Alloy

Haoliang Huang (1), Guang Ye (1,2) and Denis Damidot (3)

STUDY OF SINTERING OF GRADUAL POROUS STRUCTURES OBTAINED BY GRAVITATIONAL SEDIMENTATION

MICROSTRUCTURE-BASED SIMULATION OF TIME-DEPENDENT CHLORIDE DIFFUSIVITY IN SATURATED CEMENT PASTE

Analysis of thermal properties of cement paste during setting and hardening

THE BURNING RATE OF ALUMINIUM PARTICLES IN NITROMETHANE IN CYLINDER TESTS

HYDRATION AND MICROSTRUCTURE DEVELOPMENT OF PORTLAND CEMENT BLENDED WITH BLAST FURNACE SLAG

Modeling and Simulation of Downdraft Biomass Gasifier

Performance of ternary blended cement systems suitable for ultrahigh strength concrete

Lesson 3 How-To Session

6. DENSIFICATION BY ULTRA-HIGH PRESSURE SINTERING (UHP)

Lattice Boltzmann simulation of the ionic diffusivity of cement paste

Phase Transformation in Materials

Effect of Medium Viscosity on Breakage Parameters of Quartz in a Laboratory Ball-Mill

Thermodynamics and Microstructure: Recent Examples for Coupling of Thermodynamic and Mobility Data to the Software MICRESS

Effect of titanium additions to low carbon, low manganese steels on sulphide precipitation

EXPERIMENTAL & NUMERICAL STUDY OF CERAMIC BREEDER PEBBLE BED THERMAL DEFORMATION BEHAVIOR. Zhiyong An, Alice Ying, and Mohamed Abdou

Reducing the Cost of Hydrate Management by Under-Dosing Thermodynamic Inhibitors

Lecture 20: Eutectoid Transformation in Steels: kinetics of phase growth

Densification and grain growth of TiO 2 -doped ZnO

Effects of Lead on Tin Whisker Elimination

Computational Modeling (CFD) of Entrained Flow Gasification Kinetics with focus on the Structural Evolution of Char Particles

SP2 Report on. Service Model of Calcareous Aggregate Cement Based on Field Test. Author and Chief Investigator: M. Valix

MICROSTRUCTURE AND DURABILITY OF SELF-COMPACTING CONCRETES CONTAINING PP FIBRES

1. Formation and Growth of Ice Crystals

CHAPTER 12. Phase Transformations

INFLUENCE OF PARTICLE SIZE DISTRIBUTION OF SLAG, LIMESTONE AND FLY ASH ON EARLY HYDRATION OF CEMENT ASSESSED BY ISOTHERMAL CALORIMETRY

Studies on Main Properties of Ternary Blended Cement with Limestone Powder and Microsilica

STRENGTHENING MECHANISM IN METALS

Numerical modelling of the solidification of ductile iron

Damage Identification in Creep of Aluminium Alloy 2650-T8

Volume Change from Materials to Cell Level and Its Influence on Battery Lifetime

Nuclear Fuel Engineering (2. Modeling) Department of Nuclear Eng. KHU Kwnagheon Park

24th European Photovoltaic Solar Energy Conference and Exhibition, September 2009, Hamburg, Germany

Superhigh Strength Metal Injection Molded Low Alloy Steels by In-Process Microstructural Control

Date 30 Jan 10. Period of Performance: 02/25/ /03/2009

TENSILE CREEP MODEL BASED ON CORROSIVE ATTACK OF WATER VAPOR ON C-S-H GEL AFFECTED BY SELF-DESICCATION AND APPLIED STRESS

5. INVESTIGATION OF POROSITY IN THE PASTILLES

The Graduate University for Advanced Studies, Oroshi-cho, Toki , Japan 2

MODELING CHLORIDE TRANSPORT IN CRACKED CONCRETE --- A 3-D IMAGE

University of Pretoria Z Tang (2006) Chapter 8 Studies of acicular ferrite by thin foil TEM

Transcription:

Nucleation and growth kinetics and the density of C-S-H -Shashank Bishnoi & Karen L. Scrivener

About μic Stands for Microstructure A modelling platform for resolution-free modelling of cement microstructure Allows users to define materials, particle types, reactions and models Enables studying hypothesis through customised simulations of cement hydration Available for free in open source http://www.micthemodel.org 2

Here we use μic to study nucleation and growth kinetics 3

Nucleation and growth Simple 3D nucleation and growth: growth surface available 4

Inputs Rate of nucleation dn =k k 0 dt Rate of growth dm dr free surface =constant dt dt 5

Result vs. Avrami equation Fraction fill =1 e n kt Parameters calculated from input; no fitting needed. 6

Moving closer to cement... Random nucleation and growth on surface of spherical particles Similar nucleation and growth dn =k k 0 dt dm dr free surface =constant dt dt 7

Moving closer to cement... 8

Calculated rates Fitting needed; parameters not related to inputs 9

Calculated rates Fitting needed; parameters not related to inputs 10

This means 11 The Avrami equation does not work for alite-like systems Overlap between nuclei growing on the same particle can stop acceleration Only overlap between nuclei from different particles can lead to deceleration

What does this mean for alite? We studied the hydration rates of alites of different particle size distributions* Different models of hydration kinetics were used to reproduce the measured calorimetry curves *All experimental data from Mercedes Costoya 12

Particle size distributions *All experimental data from Mercedes Costoya 13

Measured calorimetry curves 14 *From Mercedes Costoya

Nucleation and growth 15

Important assumptions The Nucleation and Growth process is demand based: 16 Reactants are available in sufficient amounts in the solution Rate is governed only by the surface available for growth

When we fit N&G kinetics Instead of having actual nuclei, we simulate them numerically We derived an equation to calculate the fraction of surface covered and got... well... the Avrami equation again! Include an outwards growth rate and integrate in 3D for each particle... r 0 G 2 t mi= r0 17 r r 0 4 r 1 exp k 1 t G2 2 n f dr free

The fits 18

Snapshot at peak And these are the outer boundaries of the rough surfaces 19

Fit factors Fraction t1/2(hours) n G2(μm/hour) α0(%) A-38 μm 6.5 3.0 0.0044 3.6 B-83 μm 6.9 3.0 0.0315 2.5 C-38 μm 5.8 3.0 0.0290 2.1 D-18 μm 6.4 3.0 0.0215 2.5 1 Only t2/3 and G2 are fit factors 20 E-15 μm 6.3 3.0 0.0058 4.7

Diffusion regime One of the explanations of the deceleration is diffusion controlled hydration dr in = dt 21 k diff 1 1 r r in r out 2 in

Still we try to fit... 22

Fit parameters Fraction k1 (hours-n) n kdiff (μm2/h) A-38 μm 1.25 10-4 2.6 3.20 10-3 B-83 μm 5.60 10-4 2.6 3.80 10-2 C-38 μm 6.70 10-4 2.6 2.40 10-2 D-18 μm 4.50 10-4 2.6 1.60 10-2 E-15 μm 1.54 10-4 2.6 3.20 10-3 A large variation in transport properties of C-S-H has to be assumed 23

Heat-rate vs. thickness of product 24

Why not diffusion from peak? 25 A large variation in transport properties has to be assumed when density is constant Very little product present Particle surface is not fully covered if nucleation and growth on cement particles is assumed

Why doesn't this work? 26 Too little product at peak to have reduction in growth area due to overlaps Diffusion controlled process seems unlikely The acceleration can be modelled but post-peak behaviour can't be modelled

So let's try a lower density product We assume that the product formed has a low density (dry bulk density) at first It grows outwards due to a surface growth process Its packing improves with time First order assumption: 27 The rate of improvement of packing reduces exponentially with density

This is what it looks like 28

Product around a single particle: r0 G 2 t mi= r0 r r 0 4 r 1 exp k 1 t G2 2 n r f free dr o k den t r = max max min exp max min 29

The fits 30

Fit factors Fraction t1/2 (hours) n G2 (μm/hour) kden (g/cm3/hour) ρmin (g/cm3) α0 (%) A-38 μm 4.9 3.0 0.032 0.007 0.22 3.2 B-83 μm 6.9 3.0 1.10 0.0020 0.100 2.20 C-38 μm 6.2 3.0 0.77 0.0056 0.11 2.30 D-18 μm 7.4 3.0 0.35 0.012 0.185 3.15 E-15 μm 5.2 3.0 0.039 0.01 0.222 4.8 ρmin (bulk dry density) is low ~0.2 g/cm3 G2 shows a wide spread... are the fits meaningless or can it mean something? 31

The most variable factor This means the product spreads faster in systems where inter-particle distances are larger 32

Redundancy in parameters Fraction D-18 μm t1/2 (hours) n G2 (μm/hour) kden (g/cm3/hour) ρmin (g/cm3) α0 (%) 7.4 3.0 0.35 0.012 0.185 3.15 1 Two sets of parameters, similar curves 33 D-18 μm alternative 8.8 3.0 0.70 0.0115 0.145 -

Snapshot at peak... Only outer boundary of growth shown 34

Results indicate 35 A loosely packed product is formed The product forms a fine mesh in the microstructure and fills a large part of the microstructure within a few hours The packing of the product improves with time

Evidence to support Different densities of C-S-H (Jennings 2004) No capillary pores observed in NMR (Halperin et al. 1994) Setting when very little product is formed Why not seen in SEM? 36 Drying will collapse the fine, water-filled mesh of product

Low-density in micrographs 37 De Jong et al. 1967

Low-density in micrographs 38 Richardson 1999

Low-density in micrographs 39 Mathur 2007

High-resolution SEM 40 From Patrick Juilland

To conclude (1/2) 41 Nucleation and growth can explain the acceleration Post-peak behaviour is not explained Large variations in transport properties have to be assumed to explain using diffusion mechanism The formation of a low-density product spreading outwards and densifying with time can reproduce the experimental results

To conclude (2/2) We currently do not have conclusive evidence... but the results point towards a direction to investigate Can explain various other phenomena: 42 Early setting when the volume of products is small Visco-elastic behaviour Invisible capillary pores in NMR

Thank you! Available in open source http://www.micthemodel.org 43

Homogenous nucleation and growth N0 I G k n Sim. A 0 10-4 0.05 1.31 10-8 4 Sim. B 100 0 0.05 5.24 10-6 3 44

Boundary nucleation and growth Simulation Final number of nuclei Sim. C Sim. D 45 I 79,795 0.005 1,643,311 Avrami eq. G S k1 n BN eq. I 0.02 0.43 4.04 10-8 3.62 0.00175 0.05 0.005 0.43 3.17 10-8 3.24 G S 0.02 1.15 0.038 0.005 0.53

PSDs used Name A B C D E Dmode Ds-vmd Has Dv10 (μm) (μm) fines (μm) 38.5 3.47 Yes 1.7 82.6 71.0 No 47.5 38.5 32.2 No 20.4 17.9 11.9 No 6.3 15.4 4.17 Yes 2.0 Dv50 (μm) 20.0 69.5 32.4 13.8 10.3 Dv90 (μm) 59.3 95.7 47.3 24.5 20.3 Blaine (m2/kg) 190.5 61.0 121.2 239.3 305.9 BET (m2/kg) 597.7 376.8 1033.7 1537.7 N.A. 1 Fraction A-38 μm No. of particles 2034071 Size (μm) 100 1 46 B-83 μm 241 400 C-38 μm 244 175 D-18 μm 2173 100 E-15 μm 805725 75

Simulations with diffusion equation Fraction k1 (hours-n) n kdiff (μm2/h) t0 (hours) α0 (%) hp,min (μm) hp,max(μm) hp,mean (μm) 47 A-38 μm 1.25 10-4 2.6 3.20 10-3 0.0 2.3 0.02 0.16 0.10 B-83 μm 5.60 10-4 2.6 3.80 10-2 0.0 2.0 0.68 0.71 0.69 C-38 μm 6.70 10-4 2.6 2.40 10-2 0.0 1.3 0.48 0.51 0.49 D-18 μm 4.50 10-4 2.6 1.60 10-2 0.0 0.9 0.08 0.43 0.40 E-15 μm 1.54 10-4 2.6 3.20 10-3 0.0 3.0 0.0006 0.14 0.11

Dependence on parameters 48

Equations... n f =1 exp k 1 t [ [ G t f =1 exp S 0 2 3 3 G t 2y 1 exp I y 2 t 3 3G dv dv * = 1 V V =1 exp V * dt dt 49 ] dy ]