OMC 热化学：使用仿真进行精确的热量和物料平衡建模.pdf

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1、Precise Modeling Using Customization within APSPATRICK VINCENTLow-cost,low-carbon hydrogen&syngas using heat and globally abundant materials3OMC ThermochemistryCOMPLETED WORKPILOTCOMMERCIAL&GROWTH6 mos18 mos$11 million in non-dilutive grants&PhD-led developmentSERIES AFounded 2021Britt BougheyMBA,MS

2、,PEKent WarrenPhDJuan IngaPhD,PEJayaveera MuthusamyPhDPatrick VincentLiam TaylorExisting H2Production Technologies4LegacyEmergingSteam Methane ReformingElectrolysisAutothermal ReformingCO2EmissionsHighNone*LowEnergy Efficiency60-70%70-80%60-70%Cost$Large-ScaleNeeds many small unitsChemistryCH4+H2O3H

3、2+H2OH2+O2CH4+O2+H2O3H2+*assumes renewable electricity is usedThe OMC Oxygen Carrier PlatformIron&aluminumEasily fluidizable,highly spherical powderMechanically durable;highly resistant to poisons/foulingNo unwanted side reactions for H2/syngas productionFCC Fluidized Catalytic CrackerThe OMC Proces

4、s for Green H2H2OH2Step 2Step 1O2+N2N2HEATMetal oxideOMCCO2EmissionsLowEnergy Efficiency90%Cost$Large-Scale(via FCC format)(Alternate Step 2)Feed steam and CO2to produce syngas(CO+H2)for upgrading into low-carbon fuelsThe OMC Process for Methane-Driven H2H2OH2Step 2Step 1CO+2H2CH4HEATOMCCO2Emissions

5、LowEnergy Efficiency85%Cost$Large-Scale(via FCC format)(Alternate Step 2)Feed steam and CO2to produce syngas(CO+H2)for upgrading into low-carbon fuelsWater Gas ShiftCO2+3H2Metal oxide8Simulation CasesSyngasHydrogenGreenMethane-DrivenGreenMethane-Driven9Modeling Proprietary Material BehaviorSolids Ci

6、rculation RateLab DataSolid Heat CapacityReaction Enthalpy10Mass Balances for Non-Stoichiometric ReactionsCold Inlet WaterSeparationDrumHeat RecoveryOxidationReactorMetal Oxide PowderSimulation:+H2ProductReductionReactorSimulation:Heat RecoveryN2 RecoveryN2,O2Pure N2Some equipmen