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Approved for public release: distribut ion s unlimited Title: A uthur(s): Submitted tu: Industrial Processing of Complex Fluids: Formulation and Modeling J. C . Scovel, CIC-3 S. Bleasdale, CIC-3 G. M. Forest, Eng. Mech. Dept., Ohio State U . S. Bechtel, Eng. Me ch. Dept., Ohio Stat e . DOE Office of Scientific and Technican Information (OSTI) DISCLAIMER This report was prepared as an a m unt of work sponsored by an agency of the United Stacts Government. Neither the United States Government nor any agency thereof, nor any o f their crnpluyccs, makes an y warranty, express or implied, or assumes any legal liability or responsi- bility for the accuracy, completeness, or usefulness of any information. apparatus, product, or process disclosed, or represents that its UM would not infringe privately owned rights. Refer- ence herein to any specific commercial product , process, or service by trade name, trademark, manufacturer, or otherwise dots not necessarily constitute or imply its endorsement, morn- mendation, or favoring by the United States Government or any agency thereof. The views and opinions of authors exprcsscd herein do no t ntccssarily state or reflect those of the United States Government or any agency thereof. Lo s Alamos NATIONAL LABORATORY Los Aiamos National Laboratoly. an affi rmative action/e qual oppor tunity employer, i s operated by th e University 01 California for the US . Department of Energy und er contract W-7405-ENG-36. By acceptance of this article. the publisher recognizes that the U.S. Government retains a nonexclusive. royalty- free license to publish or reproduce the published form of lhis conlribution. or to allow others to do so, for US . Government purposes. Los Alamos National Laboratory requests lhat t he publisher identify this article as work performed under the ausp ices 01 th e U.S. Department of Energy. Los Alamos National Laboratory strongly supports academic freedom and a researcher's right publish; a s an instituti on. however, the Laboratory does no! endorse the viewpoint o f a publication or guarantee i t s technical correctness. FamWS(lar86) ST 2629
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Approved for public release:distribution s unlimited

Title:

Authur(s):

Submitted tu:

Industrial Processing of Complex Fluids:Formulation and Modeling

J. C. Scovel, CIC-3

S.Bleasdale,

CIC-3G. M. Forest, Eng. Mech. Dept., Ohio StateU.

S. Bechtel, Eng. Mech. Dept., Ohio State U.

DOE Office of Scientific and Technican Information (OSTI)

DISCLAIMER

This report was prepared as an a m u n t of work sponsored by an agency of the United Stacts

Government. Neithe r the United Sta tes Government nor any agency thereof, nor any of their

crnpluyccs, makes an y w arranty, express or implied, or assumes any legal liability or responsi-

bility for the accuracy, completeness, or usefulness of any information. apparatus, product, orprocess disclosed, or represents that its UM would not infringe privately owned rights. Refer-

ence herein to any specific comm ercial product, process, or service by trade name, trademark,manufacturer, or otherwise dots not necessarily constitute or imply its endorsement, morn-mendation, or favoring by the United Sta tes Government or any agency thereof. The views

and opinions of authors exprcsscd herein do not ntccssarily state or reflect those of the

United State s Government or any agency thereof.

Los AlamosN A T I O N A L L A B O R A T O R Y

Los Aiamos National Laboratoly. an affirmative action/e qual opportunity employer, is operated by th e University 01 California for the US. Department ofEnergy und er contract W-7405-EN G-36. By ac ceptan ce of this article. the publisher recognizes that the U.S. Government retains a nonexclusive. royalty-f r ee license to publish or reprodu ce the published form of lhis conlribution. or to allow others to do so, for US . Government purposes. Los Alamos NationLaboratory requests lhat t he publisher identify this article as work performed under the ausp ices 01 the U.S. Department of Energy. Los Alamos NationalLaboratory strongly supports academic freedom and a researcher's right lo publish; a s an institution. however, the Laboratory does no! endorse theviewpoint of a publication or guarantee its technical correctness.

FamWS(la

ST2

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Portions ofthis

document may be itiegiilein electronic imRge produck Images areproduced from the best mailable original

document.

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Industrial Processing of Complex Fluids: Formulation andModel ing

James C. Scovel*and S hirley BleasddleComputing, Information, and Comm unications D ivision, Los Alamos National Laboratory

Greg M. Forest and Steve BechtelEngineering Mechanics Department, Ohio State University

AbstractThis is the final report of a three-year, Laboratory Directed Research andDevelopment (LDR D) project at the Los Alamos National Laboratory (LANL).The production of many important commercial materials involves the evolutionof a complex fluid through a cooling phase into a hardened prod uct. Textilefibers, high-strength fibers such as KEVLAR and VECTRAN, plastics,chopped-fiber compounds, and fiber optical cable are but a few examples of

suc h materials. Industry contacts for each of these m aterials are keenly awareof the physics and chemistry that dominate their manufacturing processes anddesire to replace experiments with on-line, real time m odels of these processes.Industry scientists are equally aware of a hum bling fact: solu tions to theirproblems are not jus t a matter of technology transfer, but require a fundamentaldescription and simulation of their processes that lies just beyond the currentstate of science. Th e goals of our project are to develop models that can be usedto optimize macroscopic properties of the solid product, to identify sources ofundesirable defects, and to seek boundary-temperature and flow-and-materidcontrols to optimize desired properties.

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Background and Research Objectives

Th e important elemen ts of these material processes consist of a com plex fluid, usually

with s ignificant non-Ne wtonian rheology, temperature d ependen t viscosity, thermal variations

from liquid to solid phase, and the m ost elusive and least understood orientation effects at

particular length scales (molecular scales in KEVLAR type materials, intermediate or

meso scales in many textile fibers and plastics, and macro scales in chopped -fiber comp ounds)

which cou ple to the thermal flow and solidification process. Internal length-scale orientation of

the finished produc t dominates the desired properties, and yet this is the weake st link from the

basic science perspective. W e note the common ality of this multiple length-scale coupling to

various materials processing problems addressed by others at Los Alamos.As a result of the complexities of these systems, significant compromises are made to

achieve the existing crud e models which fall short of their full potential-to troubleshoot

existing processes and materials, and to perfoim parameter stud ies for the design of new

* Principal Investigator, E-mail: jcs@'lanl.gov 

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materials and processes. For example, the Hoechst-Celanese Corporation uses a fiber spinning

mod el which ignores polymer orientation in the flow and then ap plies empirical relations to

infer orientation from the computed stress field. Th is orientation inform ation is then used to

predict tensile strength and optical properties of the fiber. Th is is only one of the many features

absent: transient dynamics and stability infoimation, significant gradients transverse to the

fiber axis in temperature are presumed zero, etc.

Clearly, a coupled thermal-flow-orientation-solidification mod el of this free surface

flow (and related problems) is both unavailable and highly desirable. Th e goal of this project is

to develop th e capability to predict, for examp le, the orientatio dstres s field relationship as a

function of model parameters. Such high-level models can be used to optimize macroscopic

properties of the solid product, to identify sources of undesirable defects, and to seek

bound ary, temp erature, flow and material contro ls to optimize desired properties.

Importance to LANL’s Science and Technology Base and National R& D Needs

Th e coupling of various length-scale orientation effects to flows is itself a critical basic

scientific problem. Th e added effects of temperature dependence and phase change to

solidification, with free surfaces, pose an opportunity to advance fundamental science and

simultaneously assist US industry in gaining a com petitive advantage.

basic material science efforts here at LAN L concernin g the processing of m etals and ceramics.

Although the specific physics and engineering of metals and ceramics ar e different, at the

fundam ental level they are remarkably similar: internal length-scale structures (orientation

Furtherm ore, these capabilities m ay contribu te to and gain from other industrial and

effects) couple to the macroscopic length sc ales and critically determine the desired

macroscopic properties such as strength, defects, and post-processing deformation.

R ic hard k S a r (CMS), they must m odel the melting, flow , deformation and re-solidification of

the metal, which is fundamentally influenced by the microstructure. Th e technical and

technological impact of accurate, flexible processing co des could b e dramatic. As textile and

optical cable industry con tacts have noted, a 5-1096 gain in product efficiency translates to

market domination. Demo nstration of such capabilities should encou rage industry to engage in

CRADAs to collaborate towards the develo pmen t of on-line codes to aid in the industrial

production of these advanced m aterials.

For exam ple, in the laser welding project at Los Alamos of Tony Rollet (MST-6) and

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Scientific Approach and Accomplishments

Initially, we began by concentrating on the mold filling and solidification process. In

particular a highly viscous me lt is forced into a mold and simultaneously cooled to o btain a

solid with prescribed shape. M odeling this process amounts to unders tanding how to model

and simulate solidification in the presence of slow flow in a prescribed doma in. W e have

isolated th e areas that must be understood individually and then coupled.

1. Flow of the molten polymer.

2. Heat trm sfer in the melt domain.

3. Interface mechanics.

4. Solidification of the melt.

5. He at transfer in the solid domain.

6. Thermomechanical stress and defoimation analysis of the solid.

Each of the abo ve areas will constitute a module in a driver code.

W e have searched for a finite element fluid code that can handle phase chang es and non-

Newtonian fluids. W e have found that th e code FIDAP appears to suit our needs.

W e have successfully implemented the fluid code FIDAP in two-dimensional geometry on

a quasi-steady state solidification problem in sim ple geometry.

W e began deriving equ ations coupling the orientation effects based on Erickse n's liquid

crystal models. The se equations can be simplified to standard form and at the sam e time

give qualitative theoretical characterizations of o bserved physical ph enomena.

W e derived a multiscale foimulation of complex f-luidsbased on a nonlinear state space

model w here the observation equation corresponds to the relation between the sm all scales and

the larger scale structures. Significant information is available regarding the so lutions of such

mod els for linear systems through application of the Kalman filter. Consequently, we reduced

the scope to linear systems. How ever, even then our researches show ed that little is known

about multiscale state space models. Consequently, we concentrated on the relevant elementary

unsolved problem: how to disaggregate linear time series data.

W e developed and tested a disaggregation procedure for time series data based on an

EM (expectation and m aximization) type algorithm we derived. How ever, testing this

algorithm on ARMA (auto regressive moving average) time series mod els gave m ixed results

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until we discovered the work of Al-O sh who described the likelihood function fo r the method

[13. Ou r techniques combined with maximizing th e likelihood function gav e very interesting

results as follows:

The parameters of the ARM A mo dels generating the original data can be well determined.

The actual data is not particularly well determined by this method w hen com pared to a naive

disaggreg ation technique at a pointwise level. How ever, upon compu ting autocorrelation

functions, it is observed that our technique produces d ata that is more like data from a

stochastic process of the corre ct type.

W e produced a n extensive investigation into the behavior of our algorithm in the specific

parameter regimes of AR, M A, and ARMA time series models with interesting results.

Th e relevance of these results to complex fluids is that if the pointwise stationary data is all

that is impo rtant, more naive approaches for multiscale descriptions mig ht be relevant.

However, since the relaxational modes of a complex fluid are related to how the fluid is

evolving and how th e different scales are interacting, such a technique sh ow s promise.

The next step in such an evaluation is the development of a nonlinear analogu e of th e

Kalman filter.

Publica tion

1. Bleasdale, S., Bun-,T., and J. Scovel, “Disaggregating Tim e Series Data,” Los Alamos

Nationa l Laboratory report, in preparation.

Reference

[11 Al-Osh, M ., “A Dynam ic Linear Model Approach for Disaggregating T ime SeriesData,”

Journal of Forecasting, 8 (2), 85-96 (1989).

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