PSE Challenges in Solar Research - Carnegie Mellon...

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1 PSE Challenges in Solar Research CAPD Review Sunday March 6, 2011 B. Erik Ydstie Solar grade silicon (J. Du) Float Process for Silicon Wafers (G. Oliveros Dye Sensitized Solar cells (R. Panella Solar and wind on the Grid (J. Liu) 1 1 1

Transcript of PSE Challenges in Solar Research - Carnegie Mellon...

Page 1: PSE Challenges in Solar Research - Carnegie Mellon …egon.cheme.cmu.edu/esi/docs/pdf/ESI_Ydstie.pdf1 PSE Challenges in Solar Research CAPD Review Sunday March 6, 2011 B. Erik Ydstie

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PSE Challenges in Solar Research CAPD Review Sunday March 6, 2011

B. Erik Ydstie

Solar grade silicon (J. Du) Float Process for Silicon Wafers (G. Oliveros Dye Sensitized Solar cells (R. Panella Solar and wind on the Grid (J. Liu)

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PV System Balance of system (BOS) Solar cell module + =

Crystalline silicon

Wafer production

Cell fabrication

50% of system cost

30% of module cost

Solar-grade silicon

IC supply chain

Metallurgical grade silicon

SiCl3H distillation

Decomposition Crystallization Wafer Integrated

circuit

$3-5/kg

Aim: $20/kg $40-60/kg

$40-60/kg

REC Silicon, Moses Lake, WA Fluidized Bed Si Production: 2002–2005 Pilot plant 2005–2007 Demonstration scale 2008 Commercial scale

Supply Chain for Silicon Solar Cells

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PV System Balance of system (BOS) Solar cell module + =

Crystalline silicon

Wafer production

Cell fabrication

50% of system cost

30% of module cost

Solar-grade silicon

IC supply chain

Metallurgical grade silicon

SiCl3H distillation

Decomposition Crystallization Wafer Integrated

circuit

$3-5/kg

Aim: $20/kg $40-60/kg

$40-60/kg

REC Silicon, Moses Lake, WA Fluidized Bed Si Production: 2002–2005 Pilot plant 2005–2007 Demonstration scale 2008 Commercial scale

Supply Chain for Silicon Solar Cells

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Fluid Bed ReactorContinuous ProcessLarge surface area650 C

Si powderH2

Si

HEAT

HEAT

SiH4H2

increase throughput Reduce energy cost

The proposed solution Design and Control of Solar Silicon FBR processFrom Silane to Solar Silicon

Ron Reis REC Silicon, Paul Ege Reactech 2 PhD students

Goal: develop scale-up and control models to optimize granular yield and control particle size.

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Particles are well-mixed

Integrate over time for particle size

distribution

Multi-scale model paradigm

Computational fluid dynamics

Plug flow reactor

Population balance Bed temperature

Bed density Granular

yield

Particle size

Control fluidization regime

Simulate to obtain model input

Gas and powder are plug flow

Integrate over height for granular yield

Dust Yield loss

Operation challenges

  Fast dynamics – fluidization, reaction   Slow dynamics – particle size distribution   Distributed parameters

  Particle size distribution   Chemical reaction, yield loss   Bed fluidization

Multi-scale Modeling Approach

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CFD model for fluidization Momentum and energy balance modeled using Fluent and COMSOL multi-physics

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•  Solid phase is well mixed •  Gas phase exhibits

•  pressure gradients •  concentration gradients •  temperature gradients

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Model Verification using Pilot Plant Data

Time constant for particle size distribution about 50 hours. Weak control of distribution function Difficult to control yield loss (sensitive system)

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Model Validation and Scale-up

Y-Yield S-silane feedrate D- average diameter(p - product, s-feed) n- particle feedrate (p -product, s-feed)

Scale-up models: from pilot to demonstration plant

Full Scale Production on Moses Lake in 2009

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Summary

Acknowledgements

•  NSF Graduate Research Fellowship Program •  REC Silicon •  Reactech Process Development Inc.

Ground Breaking August 2006

Sept. 2008 Mar. 2008

Production Nov. 2009

•  Multi-scale modeling –  Captures physics of system (CFD,

Chemistry, Population balance) –  Useful for scale-up and design –  Predicts process dynamics

•  “Natural Discretization” of population balance

•  New closure relation •  Stability and control (Juan Du) •  REC Silicon's $970 million expansion

project in Moses Lake houses 24 fluid bed reactors to produce 6,500 metric tons of polysilicon per year

•  Christy’s Thesis has been “sold” from the library

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Silicon Wafers using Float Process

Edge-Defined Film Fed Growth (EFG)

Shaping die

Silicon melt Substrate

Silicon sheet

Crystal growth Ribbon

pulling

Single crystalline 18-20% Multi-crystalline 14-16% EGF etc 10-14%

Current methods are carried out in batch Continuous processes yield inferior product

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The Pilkington float Glass Process

Replaced the drawn glass process in 1960ies High throughput Low cost (capital and opearting) Very high quality glass In line processing is possible (CVD)

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2009-2013 NSF and PA Nano grants to study crystallization fluid flow and heat flow process scale-up and detailed design process control commercialization

Float Process for Silicon Wafers

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Stability of Float Process for Silicon Wafers Theory: Stability and process modeling Experiments: Water models

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Power System Frequency Control

Wind power fluctuations frequency deviation from 60Hz. Conventional generation or storage compensates wind power variations. Decentralized robust control for conventional generators Need for decentralized approaches for stability analysis and design Our Approach: Use thermodynamic stability analysis (entropy as “Lyapunov function”)