Abdul Qadir 1 , Research Assistant Peter Armstrong 2 , Associate Professor

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Abdul Qadir 1 , Research Assistant Peter Armstrong 2 , Associate Professor Mechanical Engineering Program Masdar Institute of Science and Technology Abu Dhabi, UAE IMECE2010-40571 Vancouver, BC 17 November 2010 1] [email protected] 2] [email protected] Hybrid Liquid-Air Transpired Solar Collector Model Development and Sensitivity Analysis

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Hybrid Liquid-Air Transpired Solar Collector Model Development and Sensitivity Analysis. Abdul Qadir 1 , Research Assistant Peter Armstrong 2 , Associate Professor Mechanical Engineering Program Masdar Institute of Science and Techn ology Abu Dhabi, UAE IMECE2010-40571 - PowerPoint PPT Presentation

Transcript of Abdul Qadir 1 , Research Assistant Peter Armstrong 2 , Associate Professor

Page 1: Abdul Qadir 1 , Research Assistant Peter Armstrong 2 , Associate Professor

Abdul Qadir1, Research AssistantPeter Armstrong2, Associate Professor

Mechanical Engineering ProgramMasdar Institute of Science and Technology

Abu Dhabi, UAE

IMECE2010-40571Vancouver, BC 17 November 2010

1] [email protected]] [email protected]

Hybrid Liquid-Air Transpired Solar CollectorModel Development and Sensitivity Analysis

Page 2: Abdul Qadir 1 , Research Assistant Peter Armstrong 2 , Associate Professor

Motivation: Dehumidification

UAE urban development in humid coastal regions

Abundant solar resource

Current UAE policies encourage Renewable energyEnergy efficiency

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X- xx- yy

X- xx- yy

ADWEA 2008 Daily Loads (AD Island) Weather Sensitivity

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Growth in Peak Demand

4,7905,180

5,910

7,735

8,735

9,705

10,600

11,46012,151

12,71113,139 13,452 13,716 14,089 14,340

0

2,000

4,000

6,000

8,000

10,000

12,000

14,000

16,000

2006 2007 2008 2009 2010 2011 2012 2013 2014 2015 2016 2017 2018 2019 2020

Gro

ss M

W

Abu DhabiAl AinWestern RegionTotal System

Peak electricity demand growth estimates for Abu Dhabi (2007-2012)Recent revised estimates are significantly higher

(Ref: Abu Dhabi Water and Electricity Company, 2007)

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Motivation: Dehumidification

X- xx- yy

X- xx- yy

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Conventional Solar-Powered Dehumidification

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Low-Cost Unglazed Solar Collector

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Unglazed Hybrid Liquid-Air Collector

Heated water and air to desiccant regenerator

Transpired

air

Fan

Perforated absorber plate

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Heat Balance Model

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Modeling Assumptions

1. One-Dimensional Flow of Air, Water and Heat

2. Uniform Porosity to Approximate Many Small Holes

3. T(x) Can Be Modeled By Fin EquationFin Boundary Conditions: Fluid Uniform Temperatures; Uniform AbsorbedSolar Flux

4. T(y) Can Be Modeled By Non-Linear ODE

Note That (1-3) Apply to Differential Control Volume

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Differential Control Volume Heat and Mass Balances

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Convective Heat Transfer Relations

Convection Loss From Plate (Kutscher)Face velocity, wind speed, perforation pitch

NTU-Effectiveness Model of Perforations (Kutscher)

Convective coupling of Plate to Airstream BehindNon-uniform temperature difference: bracketing analysisPitch>>BL thickness use standard flat plat Nu=f(Re,Pr,D/L)Pitch<<BL thickness assume no coupling

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Sensitivity Analysis

Ratio of Air to Total Thermal Capacitance Rate

Total Thermal Capacitance Rate

Absorber Emissivity

Back Coupling

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Sensitivity Analysis

0

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Effici

ency

mdotcp ratio

mdotcptot=25W/m2K mdotcptot=20W/m2K mdotcptot=15W/m2K

mdotcptot=10W/m2K mdotcptot=5W/m2K

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Sensitivity Analysis

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0 0.2 0.4 0.6 0.8 1

Effci

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mdotcp ratio

mdotcptot=25W/m2K mdotcptot=20W/m2K mdotcptot=15W/m2K

mdotcptot=10W/m2K mdotcptot=5W/m2K

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Sensitivity Analysis

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0 0.2 0.4 0.6 0.8 1

Twou

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mdotcp ratio

mdotcptot=25W/m2K mdotcptot=20W/m2K mdotcptot=15W/m2K

mdotcptot=10W/m2K mdotcptot=5W/m2K

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Sensitivity Analysis

300

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0 0.2 0.4 0.6 0.8 1

Twou

t

mdotcp ratio

mdotcptot=25W/m2K mdotcptot=20W/m2K mdotcptot=15W/m2K

mdotcptot=10W/m2K mdotcptot=5W/m2K

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Sensitivity Analysis

0

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effici

ency

(Ti-Ta)/G

e=0.1 e=0.5 e=0.9

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Sensitivity Analysis

0

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0 0.02 0.04 0.06 0.08 0.1 0.12

effici

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(Ti-Ta)/G

e=0.1 e=0.5 e=0.9

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Sensitivity Analysis

0

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0 0.02 0.04 0.06 0.08 0.1 0.12

effici

ency

(Ti-Ta)/G

e=0.1 e=0.5 e=0.9

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Sensitivity Analysis

0

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0 0.02 0.04 0.06 0.08 0.1 0.12

effici

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(Ti-Ta)/G

e=0.1 e=0.5 e=0.9

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Sensitivity Analysis

0

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0 0.02 0.04 0.06 0.08 0.1 0.12

effici

ency

(Ti-Ta)/G

e=0.1 e=0.5 e=0.9

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Sensitivity Analysis

0

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0 0.02 0.04 0.06 0.08 0.1 0.12

effici

ency

(Ti-Ta)/G

e=0.1 e=0.5 e=0.9

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Sensitivity Analysis

-0.6

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Effici

ency

(Ti-Ta)/G

Vw=5m/s Vw=3m/s Vw=0m/s Linear (Vw=5m/s) Linear (Vw=3m/s) Linear (Vw=0m/s)

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Sensitivity Analysis

0

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-0.05 0 0.05 0.1 0.15 0.2

Effici

ency

(Ti-Ta)/G

Vw=5m/s Vw=3m/s Vw=0m/s Linear (Vw=5m/s) Linear (Vw=3m/s) Linear (Vw=0m/s)

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Future Work

Experimental Verification

Regenerator and Absorber Models

System Optimization

Model Refinement and Collector Optimization

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X

Heated water and air to desiccant regenerator

Transpired Air

Fan

Perforated absorber plate

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Unglazed Transpired Air Collector(UTAC) for Desiccant RegenerationAdvisor: Dr. Peter Armstrong Student: Abdul Qadir

Research Objectives-Develop through simulation and testing, an UTAC which can deliver an outlet air temperature of 70˚C in order to regenerate a desiccant for desiccant cooling and dehumidification cycles.

- Investigate a hybrid UTAC to produce hot water & air.

- Develop an integrated model and test the performance of a desiccant cooling cycle coupled with a UTAC.

Broader Impacts- Could replace the gas burners which are

currently used to regenerate desiccants. - Cost effective way to integrate solar

technology to an existing cooling infrastructure.

- Can significantly reduce the electricity consumption by removing latent cooling load from the cooling system, especially in humid climates like Abu Dhabi’s.

Figure 2: Initial TRNSYS simulation resultsFigure 1: Schematic of the UTAC configuration

Heated air to desiccant cycle

Transpired Air

FanBuilding Roof

Perforated absorber plate

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Heated air to desiccant cycle

Transpired Air

FanBuilding Roof

Perforated absorber plate