SlideShare a Scribd company logo
1 of 1
Download to read offline
Heat	Transfer	in	a	Rotary	Drum	via	Conduc6on,	Convec6on,	and	Radia6on	
Brandon	Boepple,	Chemical	Engineering	
Mentor:	Dr.	Heather	Emady,	Assistant	Professor	
School	for	Engineering	of	MaDer,	Transport,	&	Energy	
How	is	heat	transfer	in	a	rotary	drum	affected	by	opera6ng	parameters	such	as	granular	fill	level	and	drum	rota6on	rate?		
Heat	transfer	occurs	via	3	modes:	conduc6on,	convec6on,	and	radia6on.	A	
general	equa6on	for	total	heat	transfer	is:	
	
In	 this	 applica6on,	 heat	 is	 transferred	 through	 wall-par6cle,	 par6cle-
par6cle,	 wall-air,	 and	 par6cle-air	 contacts.	 First,	 we	 will	 complete	
experiments	 for	 conduc6on	 hea6ng	 through	 wall-par6cle,	 wall-air,	 and	
par6cle-par6cle	 contacts.	 The	 drum	 will	 be	 heated	 externally	 and	 is	
assumed	 to	 be	 sealed	 so	 that	 convec6on	 effects	 can	 be	 neglected.	 By	
opera6ng	below	roughly	600	K,	effects	from	radia6on	are	also	neglected.	
From	this	first	round	of	experiments,	we	can	calculate	Qcond.	
	
Next,	 we	 will	 perform	 experiments	 to	 study	 convec6on	 hea6ng	 by	
inser6ng	hot	air	into	the	drum	via	a	hole	in	the	viewing	window.	From	this	
round	of	experiments,	we	can	calculate	Qconv	from	Qtot	-	Qcond.	
	
Lastly,	we	will	consider	hea6ng	via	radia6on	by	opera6ng	at	temperatures	
above	600	K.	From	this	round	of	experiments,	we	can	calculate	Qrad	from	
Qtot	– Qcond	– Qconv.	
	
These	 values	 of	 heat	 transfer	 coefficients	 will	 be	 calculated	 from	 heat	
balance	 equa6ons;	 the	 following	 example	 equa6on	 is	 a	 heat	 balance	
between	the	drum	wall	and	granular	bed.	Values	of	αs	can	be	calculated	
from	the	slope	of	the	best-fit	line	from	the	graph	of	ln(T)	vs.	6me.	
	
	
	
Qtot	=	Qcond	+	Qconv	+	Qrad	
Methodology	
Future	Work	Experimental	Setup	
Acknowledgements	
Chaudhuri	et	al.,	Experimentally	validated	computa6ons	of		
heat	transfer	in	granular	materials	in	rotary	calciners,	
Powder	Technology	198	(2010).	
Manogna	Adepu,	Graduate	Research	Associate	
•  The	drum	is	3	in.	long	with	an	inner	diameter	of	6	in.	
•  Stainless	steel	(common	in	industry).	
•  The	blue	circle	is	the	air	inlet	hole.	
•  The	green	circles	are	the	exhaust	holes.	
•  The	red	surrounds	the	10	thermocouple	inlet	holes.	
•  The	front	window	is	a	sapphire	material	that	can	
withstand	600+	K	for	infrared	viewing	purposes.	
Rollers	 for	 rota6ng	 the	
drum.	
2	heat	guns	will	be	used	
to	 heat	 the	 drum.	 They	
can	reach	temperatures	
up	to	900	K.	
Thermocouple	 (boDom),	
wireless	 transmiDer	
(led),	and	receiver	(right)	
will	 be	 used	 to	 collect	
temperature	data.	
3mm	 silica	 beads,	 a	
common	 catalyst	 in		
many	industries.	
•  Conduct	experiments	to	quan6fy	all	3	heat	transfer	
mechanisms.	
•  Inves6gate	the	effects	of	fill	level	and	rota6on	rate.	
•  A	DOE	chart	for	the	conduc6on	experiments	is	shown	
below,	including	a	total	of	48	experiments.	
		
The	mass	required	for	each	fill	
level	was	calculated	using	the	
following	equa6on:	
	
Mass=(Fill	level)*Φ*ρ*π*R2*L	
	
where	Φ	is	solids	frac6on,	ρ	is	
density	of	par6cles,	R	is	radius	
of	 drum,	 and	 L	 is	 length	 of	
drum.	
	
Fill	Level	 Mass	(g)	
10% 213.6	
15% 320.4	
20% 427.2	
25% 534.0	
S.No	 Fill	level	
RotaCon	
speed	 Trial	
		 (%)	 (rpm)	 1	 2	 3	
1	 10	 1	 1101	 2101	 3101	
2	 10	 5	 1105	 2105	 3105	
3	 10	 10	 11010	 21010	 31010	
4	 10	 20	 11020	 21020	 31020	
5	 15	 1	 1151	 2151	 3151	
6	 15	 5	 1155	 2155	 3155	
7	 15	 10	 11510	 21510	 31510	
8	 15	 20	 11520	 21520	 31520	
9	 20	 1	 1201	 2201	 3201	
10	 20	 5	 1205	 2205	 3205	
11	 20	 10	 12010	 22010	 32010	
12	 20	 20	 12020	 22020	 32020	
13	 25	 1	 1251	 2251	 3251	
14	 25	 5	 1255	 2255	 3255	
15	 25	 10	 12510	 22510	 32510	
16	 25	 20	 12520	 22520	 32520	
Future	experiments	may	also	include	the	use	of	an	infrared	
camera	 to	 gather	 temperature	 data	 while	 the	 process	 is	
running.	This	would	enhance	the	accuracy	of	the	results.	
IntroducCon	
Rotary	 drums	 have	 many	 industrial	 applica6ons	 with	 granules,	 but	
granules	 don’t	 behave	 like	 conven6onal	 solids,	 liquids,	 or	 gases	 which	
makes	these	processes	difficult	to	model	and	op6mize.	The	purpose	of	this	
research	is	to	quan6fy	all	three	modes	of	heat	transfer	in	the	granular	bed	
and	study	which	modes	dominate	under	varying	opera6ng	condi6ons.

More Related Content

What's hot

AP Physics - Chapter 13 Powerpoint
AP Physics - Chapter 13 PowerpointAP Physics - Chapter 13 Powerpoint
AP Physics - Chapter 13 Powerpoint
Mrreynon
 
modes of heat transfer, effect of temperature, cylindrical component
modes of heat transfer, effect of temperature, cylindrical component modes of heat transfer, effect of temperature, cylindrical component
modes of heat transfer, effect of temperature, cylindrical component
sajan gohel
 
gas laws in anesthesia
gas laws in anesthesiagas laws in anesthesia
gas laws in anesthesia
Vkas Subedi
 

What's hot (20)

AP Physics - Chapter 13 Powerpoint
AP Physics - Chapter 13 PowerpointAP Physics - Chapter 13 Powerpoint
AP Physics - Chapter 13 Powerpoint
 
concept of reentry heating
concept of reentry heatingconcept of reentry heating
concept of reentry heating
 
Thermal and Electrical conductivity of metals
Thermal and Electrical conductivity of metalsThermal and Electrical conductivity of metals
Thermal and Electrical conductivity of metals
 
Thermal Conductivity
Thermal ConductivityThermal Conductivity
Thermal Conductivity
 
Heat transfer
Heat transferHeat transfer
Heat transfer
 
modes of heat transfer, effect of temperature, cylindrical component
modes of heat transfer, effect of temperature, cylindrical component modes of heat transfer, effect of temperature, cylindrical component
modes of heat transfer, effect of temperature, cylindrical component
 
HEAT TRANSFER : Introduction
HEAT TRANSFER : Introduction HEAT TRANSFER : Introduction
HEAT TRANSFER : Introduction
 
Gas laws and its implications in Anaesthesiology
Gas laws and its implications in AnaesthesiologyGas laws and its implications in Anaesthesiology
Gas laws and its implications in Anaesthesiology
 
Thermal conductivity presentation
Thermal conductivity presentationThermal conductivity presentation
Thermal conductivity presentation
 
Heat Transfer
Heat TransferHeat Transfer
Heat Transfer
 
Heat transfer
Heat transferHeat transfer
Heat transfer
 
Convection of heat transfer
Convection of heat transferConvection of heat transfer
Convection of heat transfer
 
Thermal and electrical conductivity of metal
Thermal and electrical conductivity of metal Thermal and electrical conductivity of metal
Thermal and electrical conductivity of metal
 
MSc abstract
MSc abstractMSc abstract
MSc abstract
 
Introduction and Basic Modes of Heat Transfer
Introduction and Basic Modes of Heat TransferIntroduction and Basic Modes of Heat Transfer
Introduction and Basic Modes of Heat Transfer
 
Heat transfer mechanisms 1
Heat transfer mechanisms 1Heat transfer mechanisms 1
Heat transfer mechanisms 1
 
2. ataee2015
2. ataee20152. ataee2015
2. ataee2015
 
HEAT TRANSFER
HEAT TRANSFERHEAT TRANSFER
HEAT TRANSFER
 
Heat transfer
Heat transferHeat transfer
Heat transfer
 
gas laws in anesthesia
gas laws in anesthesiagas laws in anesthesia
gas laws in anesthesia
 

Viewers also liked

Fertilizer analysis
Fertilizer analysisFertilizer analysis
Fertilizer analysis
Akma Ija
 
Fertilizer analysis presentation
Fertilizer analysis presentationFertilizer analysis presentation
Fertilizer analysis presentation
Akma Ija
 
Soil analysis
Soil analysisSoil analysis
Soil analysis
Akma Ija
 
LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1
LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1
LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1
Titin Indrawati
 
Pemilihan alat dan mesin pertanian (timeliness cost)
Pemilihan alat dan mesin pertanian (timeliness cost)Pemilihan alat dan mesin pertanian (timeliness cost)
Pemilihan alat dan mesin pertanian (timeliness cost)
Iqrimha Lairung
 

Viewers also liked (18)

AVK ENERTECH 2016
AVK ENERTECH 2016AVK ENERTECH 2016
AVK ENERTECH 2016
 
Acara I
Acara IAcara I
Acara I
 
Maquinas compactadoras
Maquinas compactadorasMaquinas compactadoras
Maquinas compactadoras
 
Laporan tugas besar
Laporan tugas besarLaporan tugas besar
Laporan tugas besar
 
Tugas 1
Tugas 1Tugas 1
Tugas 1
 
Pertemuan 5a gerbang kombinasi-maxtem-minterm
Pertemuan 5a   gerbang kombinasi-maxtem-mintermPertemuan 5a   gerbang kombinasi-maxtem-minterm
Pertemuan 5a gerbang kombinasi-maxtem-minterm
 
Fertilizer analysis
Fertilizer analysisFertilizer analysis
Fertilizer analysis
 
Fertilizer analysis presentation
Fertilizer analysis presentationFertilizer analysis presentation
Fertilizer analysis presentation
 
Csec social studies sba
Csec social studies sbaCsec social studies sba
Csec social studies sba
 
Moa of antimicrobials
Moa of antimicrobialsMoa of antimicrobials
Moa of antimicrobials
 
03 dasar sistem komputer
03 dasar sistem komputer03 dasar sistem komputer
03 dasar sistem komputer
 
New microsoft office power point presentation
New microsoft office power point presentationNew microsoft office power point presentation
New microsoft office power point presentation
 
Soil analysis
Soil analysisSoil analysis
Soil analysis
 
Sosialisasi Keamanan Informasi_Sektor Kesehatan
Sosialisasi Keamanan Informasi_Sektor KesehatanSosialisasi Keamanan Informasi_Sektor Kesehatan
Sosialisasi Keamanan Informasi_Sektor Kesehatan
 
Sosialisasi Keamanan Informasi_Bidang Mineral dan Batubara
Sosialisasi Keamanan Informasi_Bidang Mineral dan BatubaraSosialisasi Keamanan Informasi_Bidang Mineral dan Batubara
Sosialisasi Keamanan Informasi_Bidang Mineral dan Batubara
 
LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1
LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1
LAPORAN PRAKTIKUM PINDAH PANAS ACARA 1
 
Half adder & full adder
Half adder & full adderHalf adder & full adder
Half adder & full adder
 
Pemilihan alat dan mesin pertanian (timeliness cost)
Pemilihan alat dan mesin pertanian (timeliness cost)Pemilihan alat dan mesin pertanian (timeliness cost)
Pemilihan alat dan mesin pertanian (timeliness cost)
 

Similar to Boepple, Brandon

1-s2.0-S0017931016319998-main
1-s2.0-S0017931016319998-main1-s2.0-S0017931016319998-main
1-s2.0-S0017931016319998-main
Sanskar Panse
 

Similar to Boepple, Brandon (20)

Recent advancements heat transfer
Recent advancements heat transferRecent advancements heat transfer
Recent advancements heat transfer
 
Lecture 1
Lecture 1Lecture 1
Lecture 1
 
Separation of carbon 13 by thermal diffusion
Separation of carbon 13 by thermal diffusionSeparation of carbon 13 by thermal diffusion
Separation of carbon 13 by thermal diffusion
 
Lab%201
Lab%201Lab%201
Lab%201
 
Creating Comfortable Air Conditions in Mars for a Sample Volume Shelter
Creating Comfortable Air Conditions in Mars for a Sample Volume ShelterCreating Comfortable Air Conditions in Mars for a Sample Volume Shelter
Creating Comfortable Air Conditions in Mars for a Sample Volume Shelter
 
analysis of fins subjected to forced convection.
analysis of fins subjected to forced convection.analysis of fins subjected to forced convection.
analysis of fins subjected to forced convection.
 
1-s2.0-S0017931016319998-main
1-s2.0-S0017931016319998-main1-s2.0-S0017931016319998-main
1-s2.0-S0017931016319998-main
 
D031201025031
D031201025031D031201025031
D031201025031
 
heat transfer operation
heat transfer operationheat transfer operation
heat transfer operation
 
HEAT TRANSFER
HEAT TRANSFER HEAT TRANSFER
HEAT TRANSFER
 
electric injera baking pan efficency analsis
electric injera baking pan  efficency analsiselectric injera baking pan  efficency analsis
electric injera baking pan efficency analsis
 
Heat Transfer.pdf
Heat Transfer.pdfHeat Transfer.pdf
Heat Transfer.pdf
 
Lecture 2
Lecture 2Lecture 2
Lecture 2
 
Experimentation and analysis of heat transfer through perforated fins of diff...
Experimentation and analysis of heat transfer through perforated fins of diff...Experimentation and analysis of heat transfer through perforated fins of diff...
Experimentation and analysis of heat transfer through perforated fins of diff...
 
Effect of Geometry on Variation of Heat Flux and Drag for Launch Vehicle -- Z...
Effect of Geometry on Variation of Heat Flux and Drag for Launch Vehicle -- Z...Effect of Geometry on Variation of Heat Flux and Drag for Launch Vehicle -- Z...
Effect of Geometry on Variation of Heat Flux and Drag for Launch Vehicle -- Z...
 
The Conception, Types, and Applications of Heat Pipe Solar Collector
The Conception, Types, and Applications  of Heat Pipe Solar CollectorThe Conception, Types, and Applications  of Heat Pipe Solar Collector
The Conception, Types, and Applications of Heat Pipe Solar Collector
 
Experimental Studies on Pool Boiling Heat Transfer Using Alumina and Graphene...
Experimental Studies on Pool Boiling Heat Transfer Using Alumina and Graphene...Experimental Studies on Pool Boiling Heat Transfer Using Alumina and Graphene...
Experimental Studies on Pool Boiling Heat Transfer Using Alumina and Graphene...
 
Parametric Studies On Heat Transfer by Natural Convection from Inclined Cylin...
Parametric Studies On Heat Transfer by Natural Convection from Inclined Cylin...Parametric Studies On Heat Transfer by Natural Convection from Inclined Cylin...
Parametric Studies On Heat Transfer by Natural Convection from Inclined Cylin...
 
Heat transfer
Heat transferHeat transfer
Heat transfer
 
Heat Exchange Fundamentals for Shell and Tube Units
Heat Exchange Fundamentals for Shell and Tube UnitsHeat Exchange Fundamentals for Shell and Tube Units
Heat Exchange Fundamentals for Shell and Tube Units
 

Boepple, Brandon

  • 1. Heat Transfer in a Rotary Drum via Conduc6on, Convec6on, and Radia6on Brandon Boepple, Chemical Engineering Mentor: Dr. Heather Emady, Assistant Professor School for Engineering of MaDer, Transport, & Energy How is heat transfer in a rotary drum affected by opera6ng parameters such as granular fill level and drum rota6on rate? Heat transfer occurs via 3 modes: conduc6on, convec6on, and radia6on. A general equa6on for total heat transfer is: In this applica6on, heat is transferred through wall-par6cle, par6cle- par6cle, wall-air, and par6cle-air contacts. First, we will complete experiments for conduc6on hea6ng through wall-par6cle, wall-air, and par6cle-par6cle contacts. The drum will be heated externally and is assumed to be sealed so that convec6on effects can be neglected. By opera6ng below roughly 600 K, effects from radia6on are also neglected. From this first round of experiments, we can calculate Qcond. Next, we will perform experiments to study convec6on hea6ng by inser6ng hot air into the drum via a hole in the viewing window. From this round of experiments, we can calculate Qconv from Qtot - Qcond. Lastly, we will consider hea6ng via radia6on by opera6ng at temperatures above 600 K. From this round of experiments, we can calculate Qrad from Qtot – Qcond – Qconv. These values of heat transfer coefficients will be calculated from heat balance equa6ons; the following example equa6on is a heat balance between the drum wall and granular bed. Values of αs can be calculated from the slope of the best-fit line from the graph of ln(T) vs. 6me. Qtot = Qcond + Qconv + Qrad Methodology Future Work Experimental Setup Acknowledgements Chaudhuri et al., Experimentally validated computa6ons of heat transfer in granular materials in rotary calciners, Powder Technology 198 (2010). Manogna Adepu, Graduate Research Associate •  The drum is 3 in. long with an inner diameter of 6 in. •  Stainless steel (common in industry). •  The blue circle is the air inlet hole. •  The green circles are the exhaust holes. •  The red surrounds the 10 thermocouple inlet holes. •  The front window is a sapphire material that can withstand 600+ K for infrared viewing purposes. Rollers for rota6ng the drum. 2 heat guns will be used to heat the drum. They can reach temperatures up to 900 K. Thermocouple (boDom), wireless transmiDer (led), and receiver (right) will be used to collect temperature data. 3mm silica beads, a common catalyst in many industries. •  Conduct experiments to quan6fy all 3 heat transfer mechanisms. •  Inves6gate the effects of fill level and rota6on rate. •  A DOE chart for the conduc6on experiments is shown below, including a total of 48 experiments. The mass required for each fill level was calculated using the following equa6on: Mass=(Fill level)*Φ*ρ*π*R2*L where Φ is solids frac6on, ρ is density of par6cles, R is radius of drum, and L is length of drum. Fill Level Mass (g) 10% 213.6 15% 320.4 20% 427.2 25% 534.0 S.No Fill level RotaCon speed Trial (%) (rpm) 1 2 3 1 10 1 1101 2101 3101 2 10 5 1105 2105 3105 3 10 10 11010 21010 31010 4 10 20 11020 21020 31020 5 15 1 1151 2151 3151 6 15 5 1155 2155 3155 7 15 10 11510 21510 31510 8 15 20 11520 21520 31520 9 20 1 1201 2201 3201 10 20 5 1205 2205 3205 11 20 10 12010 22010 32010 12 20 20 12020 22020 32020 13 25 1 1251 2251 3251 14 25 5 1255 2255 3255 15 25 10 12510 22510 32510 16 25 20 12520 22520 32520 Future experiments may also include the use of an infrared camera to gather temperature data while the process is running. This would enhance the accuracy of the results. IntroducCon Rotary drums have many industrial applica6ons with granules, but granules don’t behave like conven6onal solids, liquids, or gases which makes these processes difficult to model and op6mize. The purpose of this research is to quan6fy all three modes of heat transfer in the granular bed and study which modes dominate under varying opera6ng condi6ons.