meus presentation-me 490

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Energy Substitution of Electricity with Natural Gas for Industrial Dryers Kumar Aanjaneya (graduate student) & Hayden Youngs (Senior) Completed the work Danielle Kyser (graduated) & Karl Stimmel (graduated) Started the work Advisors: Arvind Atreya ([email protected] ) & Claus Borgnakke ( [email protected] ) Department of Mechanical Engineering University of Michigan, Ann Arbor 48109 1 MEUS: ME 490 | 12/10/2015

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Page 1: MEUS PRESENTATION-ME 490

Energy Substitution of Electricity with Natural Gas for Industrial Dryers

Kumar Aanjaneya (graduate student) & Hayden Youngs (Senior)Completed the work

Danielle Kyser (graduated) & Karl Stimmel (graduated)Started the work

Advisors:Arvind Atreya ([email protected]) & Claus Borgnakke ([email protected])

Department of Mechanical EngineeringUniversity of Michigan, Ann Arbor 48109

1MEUS: ME 490 | 12/10/2015

Page 2: MEUS PRESENTATION-ME 490

Acknowledgements

• This work was sponsored by the DoE via the University of Michigan Industrial Assessment Center (IAC)

• Special thanks to:– Weiyu Cao, Yawei Chen (PhD Students), Dr. Jacek Szymczyk (Visiting

Researcher), Harald Eberhart (Glass Blower)

2MEUS: ME 490 | 12/10/2015

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Inspiration• Currently electric dryers are used in the plant• Substitution with natural gas dryers, benefits:

– Cheaper to run– Lower Carbon footprint– Faster heating; thus increased production speed

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Concerns• Temperature Control

• Factory Air Quality Issues

• Flame Stability

• Incomplete Combustion

• Pollutant Formation

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Data from the Plant• The plant uses dryers rated at 15 kW (0.05 MMBtu/hr)

• Dryers are used for 3120 hrs/year

• Cost of Electricity: $0.08/kWh (=$23.5/MMBtu)

• Cost of Natural Gas: $5.5/MMBtu

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Current Set-Up

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AirBlower

Electric Heater

Air Knife

Conveyor belt

Dry hot air jet

MEUS: ME 490 | 12/10/2015

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Proposed Set-Up

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AirBlower

Conveyor belt

Dry hot air jet

Air Knife

Combustion Air Fuel

Burner

MEUS: ME 490 | 12/10/2015

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Carbon Footprints• Combustion of Natural Gas:

– emissions per kg of Natural Gas = kg– Fuel rate for a 15 kW dryer = – production rate for the dryer = 1.08 x 2.75 = 2.97 kg/hr– Annual production = 2.97 x 3120 = 9.2 tons/year

• Similar Energy produced by a Power plant (~40% efficient ):– production rate = 23 tons/year

• A reduction of 13.8 tons/year

8MEUS: ME 490 | 12/10/2015

Hayden Youngs
check CO2 production
Hayden Youngs
may be a conservative understatement
Page 9: MEUS PRESENTATION-ME 490

Design• Co-Annular tubes for the burner1.• High velocity stream of air entrains high temperature combustion

products.• Optimum mixing to achieve uniform temperatures.

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1. Gillon, P., Chahine, M., Gilard, V., and Sarh, B. 2014. “Heat Transfer from A Laminar Jet Methane Flame in A Co-Annular Jet of Oxygen Enriched Air” Combustion Science and Technology.

MEUS: ME 490 | 12/10/2015

Hayden Youngs
Put design slides before cost savings
Page 10: MEUS PRESENTATION-ME 490

Experimental Design• Obstacles to induce turbulence and mixing2

• High levels of dilution to:– Achieve complete combustion– Achieve desired temperatures

• Burner tubes made of glass to optically determine flame color and soot formation

• Temperature measurements at three radial locations downstream

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2. Guo, P., Zang, S., and Ge, B. 2010. “Predictions of Flow Field for Circular-Disk Bluff-Body Stabilized Flame Investigated by Large Eddy Simulation and Experiments” Journal of Engineering for Gas Turbines and Power.

MEUS: ME 490 | 12/10/2015

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Experimental Design (contd.)• Current small-scale apparatus designed for 1kW capacity (0.016

g/s fuel inlet)

• Idea is to have low fuel momentum but high primary air flow momentum to promote fuel-air mixing2

• Secondary (dilution) Air Flow kept constant by using a computer fan– For 150 C (302 F) outlet temperature, flow is ~35 CFM

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2. Guo, P., Zang, S., and Ge, B. 2010. “Predictions of Flow Field for Circular-Disk Bluff-Body Stabilized Flame Investigated by Large Eddy Simulation and Experiments” Journal of Engineering for Gas Turbines and Power.

MEUS: ME 490 | 12/10/2015

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Experimental Design

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Outer TubePrimary Tube

MEUS: ME 490 | 12/10/2015

Hayden Youngs
show combustion
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FLUENT Calculations• FLUENT calculations were carried out for the design prior to

fabrication

• Simplifications made:– 2D Axisymmetric model– Neglect heat loss through walls

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Temperature Contours using FLUENT

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Hayden Youngs
take flame and put into slide 15
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Laboratory Apparatus

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• Outer Tube: 1.8” Dia

• Fuel Tube: 0.9” Dia

• Inner (Air) Tube: 0.125’ Dia

• Fuel and Inner Tubes: 2” Long

• Outer Tube: 1’ Long

MEUS: ME 490 | 12/10/2015

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Thermocouple

Computer Fan

Primary Tube

Outer Tube

Apparatus (Contd.)

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Images

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Temperature Plots

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Cost savings/dryer• Considering a 15kW dryer, running for 3120 hrs/year

• For Electricity powered dryer, annual electricity cost:– Costelec dryer = Wel x HR x Ce=15 x 3120 x 0.08= $3,750

• For gas powered dryer, annual fuel cost:– CostNG dryer = Wel x HR x CNG= 0.05 x 3120 x 5.5= $858

• Cost Savings = $2892/dryer• Here:

– Wel : Power rating (kW or MMBtu/hr)– HR: Hours of use per year (3120 hrs)– Ce: Cost of electricity ($/kWh)– CNG: Cost of electricity ($/MMBtu)

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Potential Cost Savings

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Hayden Youngs
explanation: consider putting this later in presentation
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Comments• Temperatures decreases with increase in primary air flow.

(Dilution)

• Actual temperatures are lower than predicted– Can be explained due to heat loss in the real case

• Actual mixing higher near the wall than FLUENT– Because of additional obstacles (spiders to hold the central tube)

• No evidence of soot on any surface

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Comments (Contd.)• Flame was stable.

– No flame-blowout throughout the duration of the experiments for all cases

• Calculations suggest no significant increase in humidity.– Relative Humidity increases from 3% to 4% due to additional water in the

stream produced by combustion – air still suitable for drying

• Costs of implementation– Burners cost around $1000-$1500 (15kW)– Burners would require more maintenance than electrical heaters (around

$700 per year)– With savings of $2892 per year, these costs are reasonable

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Future Work• Current prototype is a lab scale model

• Needs to be scaled up for usage in industry– Use of multiple fuel jets to achieve better mixing and combustion in higher

power regimes– Metallic burners with additional active/passive mixing enhancers

• Detailed gas analysis of exhaust

• Closer control of the flow rates

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Future Work• Increased control of flow to:

– Achieve desired temperatures– Maintain flame stability (by maintaining stoichiometric ratio)

• Flame sensor and Ignitor– Ignite the fuel at start up – Reignite if the flame blows off or turn fuel off

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Thank You!

Questions?

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