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LANL LA-UR-04-2805 Photopolymerization/Pyrolysis Photopolymerization/Pyrolysis Route to Route to Microstructured Microstructured Membrane Development Membrane Development Kathryn A. Berchtold Kathryn A. Berchtold Jennifer S. Young Jennifer S. Young Los Alamos National Laboratory Los Alamos National Laboratory Materials Science & Technology Division Materials Science & Technology Division 26 May, 2004 26 May, 2004 This presentation does not contain any proprietary or confidential information
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Page 1: Photopolymerization/Pyrolysis Route to Microstructured … · 2020. 11. 21. · LANL LA-UR-04-2805 Photopolymerization/Pyrolysis Route to Microstructured Membrane Development Kathryn

LANL LA-UR-04-2805

Photopolymerization/PyrolysisPhotopolymerization/PyrolysisRoute to Route to MicrostructuredMicrostructuredMembrane DevelopmentMembrane Development

Kathryn A. BerchtoldKathryn A. BerchtoldJennifer S. YoungJennifer S. Young

Los Alamos National LaboratoryLos Alamos National LaboratoryMaterials Science & Technology DivisionMaterials Science & Technology Division

26 May, 200426 May, 2004

This presentation does not contain any proprietary or confidential information

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LANL LA-UR-04-2805

ObjectivesObjectivesProvide a rational approach to the design of Provide a rational approach to the design of synthesis processes for robust ceramic synthesis processes for robust ceramic membranes with high gas membranes with high gas permselectivitypermselectivity. .

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LANL LA-UR-04-2805

BudgetBudgetFunding in FY04 : 200KFunding in FY04 : 200KSubtask 1a: Establishment of the membrane Subtask 1a: Establishment of the membrane

fabrication and testing capability and a fabrication and testing capability and a coarse grained approach to coarse grained approach to understanding the interrelationship understanding the interrelationship between polymer microstructure and between polymer microstructure and composition and the separation composition and the separation characteristics of the ceramic characteristics of the ceramic membrane product.membrane product.

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Technical Barriers and TargetsTechnical Barriers and TargetsDOE Technical Barriers for Hydrogen Production: DOE Technical Barriers for Hydrogen Production:

Distributed Hydrogen Production from Natural Gas or Liquid FuelsDistributed Hydrogen Production from Natural Gas or Liquid FuelsBarriersBarriers

A. Fuel Processor Capital CostsA. Fuel Processor Capital Costs

D. Carbon Dioxide EmissionsD. Carbon Dioxide Emissions

General (Cross Cutting) Hydrogen Production BarriersGeneral (Cross Cutting) Hydrogen Production Barriers

AB. Hydrogen Separation and PurificationAB. Hydrogen Separation and Purification

DOE Technical Target for Separation Membranes for Hydrogen DOE Technical Target for Separation Membranes for Hydrogen Production for 2010Production for 2010

Flux Rate 200 scfh/ftFlux Rate 200 scfh/ft22

Cost <$100/ftCost <$100/ft22

Operating Temperature 300Operating Temperature 300--600 °C600 °C

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ApproachApproachFormation of defectFormation of defect--free, robust, ceramic free, robust, ceramic membranes that will membranes that will maintain gas maintain gas productivity and productivity and selectivity to selectivity to temperatures in temperatures in excess of 1000°C excess of 1000°C Fabrication of these Fabrication of these membranes via membranes via economically viable economically viable and established and established polymer processing polymer processing techniques.techniques.

Silazane OligomericCeramic Precursor

Organic or Inorganic Comonomer

Crosslinked Polymeric Ceramic Precursor

Amorphous Ceramic

Photoinitiator(optional)

High Temperature Membranes

Crystalline Ceramic

Silazane OligomericCeramic Precursor

Organic or Inorganic Comonomer

Crosslinked Polymeric Ceramic Precursor

Crosslinked Polymeric Ceramic Precursor

Amorphous CeramicAmorphous Ceramic

Photoinitiator(optional)

High Temperature Membranes

High Temperature Membranes

Crystalline CeramicCrystalline Ceramic

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Thin Film of Liquid Phase Precursors

Polymeric Membrane ∆

Spin Coat / Cast(spin cycle conditions,

acceleration, velocity, & duration of each step in

the cycle)

UV/Vis Exposure(wavelength, environment,

intensity, initiation mechanism & rate,

temperature)

Pyrolysis(environment,

pyrolysis rate, ultimate temperature)

Amorphous / Crystalline Ceramic

Membrane

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Membrane Property ManipulationMembrane Property ManipulationMonomer Functionality Monomer Structure

Polymerization Kinetics Network Structure

Preceramic PolymerMembrane Properties

Pyrolysis Kinetics Network Structure

Ceramic MembraneProperties

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ImpactImpactFirst commercially viable production of First commercially viable production of ceramic membranesceramic membranes

Enabling technology for fuel reformingEnabling technology for fuel reforming

Reduction of parasitic losses in carbon Reduction of parasitic losses in carbon sequestration processessequestration processes

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ChallengesChallengesChallengesChallenges

Forming defect free membranesForming defect free membranes

Optimizing membrane Optimizing membrane fixturingfixturing

Optimizing processing conditions to achieve Optimizing processing conditions to achieve meaningful selectivity and permeabilitymeaningful selectivity and permeability

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Project SafetyProject SafetyIntegrated Work ManagementIntegrated Work Management

All processes are compliant with the LANL All processes are compliant with the LANL Integrated Work Management process. All Integrated Work Management process. All processes have had the required management processes have had the required management walkwalk--downs. All of the associated Integrated downs. All of the associated Integrated Work Documents / Hazard Control Plans have Work Documents / Hazard Control Plans have had all required reviews and all required had all required reviews and all required approvals have been obtained.approvals have been obtained.

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Project TimelineProject Timeline

Phase I Phase I –– Feasibility/Capability DevelopmentFeasibility/Capability DevelopmentA.A. Design coarse grained experimental programDesign coarse grained experimental programB.B. Select Initial Material Chemistries/Functionalities to Evaluate Select Initial Material Chemistries/Functionalities to Evaluate C.C. Establish membrane synthesis capability through the proposed proEstablish membrane synthesis capability through the proposed processing route. cessing route.

•• This capability includes all processing steps and experimental pThis capability includes all processing steps and experimental protocols necessary to rotocols necessary to produce, characterize, and test a ceramic membrane as it is prodproduce, characterize, and test a ceramic membrane as it is produced from uced from inorganic/organic photoactive precursors. Extend our high tempeinorganic/organic photoactive precursors. Extend our high temperature testing rature testing capabilities. capabilities.

Phase II Phase II –– PrePre--Ceramic Polymer and Ceramic Thin Film Development & TestingCeramic Polymer and Ceramic Thin Film Development & TestingD.D. Perform initial evaluations on a limited set of Perform initial evaluations on a limited set of preceramicpreceramic polymer precursors with polymer precursors with

dramatically different microstructures. dramatically different microstructures. •• Report results on polymer thin film material properties as a funReport results on polymer thin film material properties as a function of ction of comonomercomonomer

composition and polymerization conditionscomposition and polymerization conditionsE.E. Perform initial evaluations on amorphous ceramic thin film materPerform initial evaluations on amorphous ceramic thin film material properties as a ial properties as a

function of prefunction of pre--ceramic polymer properties and ceramic polymer properties and pyrolysispyrolysis conditions conditions •• Report results from initial ceramic material evaluations Report results from initial ceramic material evaluations

Phase III Phase III –– Amorphous Ceramic Membrane TestingAmorphous Ceramic Membrane TestingF.F. Membrane production and testingMembrane production and testing

•• Report results from initial evaluations on amorphous ceramic memReport results from initial evaluations on amorphous ceramic membrane brane permselectivitypermselectivity as as a function of prea function of pre--ceramic polymer properties, ceramic polymer properties, pyrolysispyrolysis conditions, and operating conditions, and operating temperature temperature

1/04 11/043/04 5/04 7/04 9/04A B C D FE

I II III

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Technical Accomplishments/ProgressTechnical Accomplishments/ProgressEstablished membrane synthesis capability through the proposed Established membrane synthesis capability through the proposed processing route with selected materials. processing route with selected materials.

Established Experimental DesignEstablished Experimental DesignSelected Chemistries/Materials for Initial EvaluationSelected Chemistries/Materials for Initial EvaluationIntegrated Work ManagementIntegrated Work Management

All processes are compliant with the LANL Integrated Work ManageAll processes are compliant with the LANL Integrated Work Management process. Allment process. Allprocesses have had the required management walkprocesses have had the required management walk--downs. All of the associated downs. All of the associated Integrated Work Documents / Hazard Control Plans have had all reIntegrated Work Documents / Hazard Control Plans have had all required reviews quired reviews and all required approvals have been obtained.and all required approvals have been obtained.

With a Single Formulation:With a Single Formulation:Initial film casting procedures were establishedInitial film casting procedures were establishedCast films were Cast films were photopolymerizedphotopolymerized under controlled conditionsunder controlled conditionsPolymerization kinetics monitoring and evaluation protocols werePolymerization kinetics monitoring and evaluation protocols were established and established and testedtestedControlled Controlled PyrolysisPyrolysis Capability was EstablishedCapability was Established

Multiple atmospheres including reactive environments can be usedMultiple atmospheres including reactive environments can be usedTemperature range: ambient to 1700 °CTemperature range: ambient to 1700 °CControl of temperature ramps, soaks, and gas switching during Control of temperature ramps, soaks, and gas switching during pyrolysispyrolysis

Protocols and equipment are in place for TGA, MS, and FTIR evaluProtocols and equipment are in place for TGA, MS, and FTIR evaluation of the ation of the pyrolysispyrolysis processprocess

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Technical Accomplishments/ProgressTechnical Accomplishments/Progress

Established membrane synthesis capability through the proposed Established membrane synthesis capability through the proposed processing route with selected materials. processing route with selected materials.

A membrane fixture for high temperature (ambient A membrane fixture for high temperature (ambient –– 800 °C) permeation testing800 °C) permeation testing of ceramic membrane films has been designed and constructedof ceramic membrane films has been designed and constructedSingle gas and multiSingle gas and multi--gas permeation test rigs are in place for membrane gas permeation test rigs are in place for membrane permselectivitypermselectivity evaluationevaluationA membrane fixture for high temperature above 800 °C has been deA membrane fixture for high temperature above 800 °C has been designed and signed and is being fabricated.is being fabricated.

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Monitor the decay in reactive functionalities and Monitor the decay in reactive functionalities and appearance of new functionalities via the change in the appearance of new functionalities via the change in the appropriate absorbance peaks over timeappropriate absorbance peaks over time

Temporal resolution: Temporal resolution: 30 ms30 ms

Obtain complete Obtain complete monomer monomer polymerpolymer

ceramic spectra ceramic spectra with timewith time

Experimental Experimental -- FTIRFTIR

Wavenumbers, cm-1

Abs

orba

nce

t = 0 sec

t = 3.5 sec

0.00

0.20

0.40

0.60

0.80

1.00

0 10 20 30 40 50 60Polymerization Time, sec

Con

vers

ion

**The spectra presented above are NOT representative of the materials utilized in this work

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HorizontalHorizontalOrientationOrientationIncreasedIncreasedControlControlRepeatabilityRepeatability

IR Source

Sample Stage/ Sample Holder (incorporating

temperature (-40 to 250°C transmission and ambient

to 1400°C gas phase during pyrolysis) and atmosphere

control)

Excitation Source Detector

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Large Scale Large Scale PhotopolymerizationPhotopolymerization for for Membrane FabricationMembrane Fabrication

Controlled Atmosphere Chamber

1000W Arc Lamp Optical Train

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Future WorkFuture WorkRemainder of FY 2004Remainder of FY 2004

Continue initial evaluations of preContinue initial evaluations of pre--ceramic polymer ceramic polymer thin film properties as a function of thin film properties as a function of comonomercomonomerconcentration on a limited set of precursors. concentration on a limited set of precursors. Perform initial evaluations on amorphous ceramic thin Perform initial evaluations on amorphous ceramic thin film material properties as a function of prefilm material properties as a function of pre--ceramic ceramic polymer properties and polymer properties and pyrolysispyrolysis conditionsconditionsAmorphous Ceramic Membrane Production & TestingAmorphous Ceramic Membrane Production & Testing

Remainder of FY 2004 Remainder of FY 2004 -- FY05 (Funding FY05 (Funding Dependant)Dependant)

Subtask 1b: Implementation of a full factorial Subtask 1b: Implementation of a full factorial experimental design to elucidate the factors that most experimental design to elucidate the factors that most significantly impact the significantly impact the permselectivitypermselectivity of the final of the final membrane productmembrane product

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FundingFundingDepartment of Energy

DOE / EERE Hydrogen Production & DeliveryLos Alamos National Laboratory

Los Alamos National Laboratory is operated by the University of California for the United States DOE under Contract W-7405-ENG-

36. This document has been designated LA-UR-04-2805.


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