Freeze Flame Nano
Presented May 4, 2006 by
Keshan Velasquez Tyler Viani
Freeze Flame Nano Presented May 4, 2006 by Keshan Velasquez - - PowerPoint PPT Presentation
Freeze Flame Nano Presented May 4, 2006 by Keshan Velasquez Tyler Viani Outline Introduction to Fires and Flame retardants Problem Statement Product Discovery Economics and Business Plan Conclusions and Recommendations
Presented May 4, 2006 by
Keshan Velasquez Tyler Viani
1 How Flame Retardants Work? EFRA. Accessed January 2006.
<http://www.cefic-efra.com/>
2 United States Fire Administration. National Fire Statistics. Accessed
January 2006. www.usfa.fema.gov/statistic/national/
1 How Flame Retardants Work? EFRA. Accessed January 2006.
<http://www.cefic-efra.com/>
charring
1 How Flame Retardants Work? EFRA. Accessed January 2006.
<http://www.cefic-efra.com/>
conjunction with another flame retardant
1 How Flame Retardants Work? EFRA. Accessed January 2006.
<http://www.cefic-efra.com/>
1 How Flame Retardants Work? EFRA. Accessed January 2006.
<http://www.cefic-efra.com/>
Coatings
45% 24% 4% 27% Halogenated Phosphorus Nitrogen Inorganics 3 Lerner, Ivan. “FR Market Down but Not Out: Albemarle Stays the Course.”
Chemical Market Reporter. December 10, 2001 p. 12.
3 Lerner, Ivan. “FR Market Down but Not Out: Albemarle Stays the Course.”
Chemical Market Reporter. December 10, 2001 p. 12.
+
Phosphate Nano-clay (Cloisite)
*http://www.users.bigpond.com/jim.chambers/Cloisite.htm
encasings
etc.
PVAc + NaOH(aq) + H2O PVOH(aq) + NaAc(aq) + H2O
C C H H H O + NaOH(aq) + H—O—H C O CH3 C C H H H OH + NaAc(aq) + H2O
n n
C C H H H OH + Polymer Slurry: N+ CH3 CH3 HT HT
C C H H H OH n δ- N+ CH3 CH3 HT HT ………. NOTE: This will not occur at every OH-site
C C H H H OH n δ- N+ CH3 CH3 HT HT ………. + RH2PO4
Polar Sites= Clay= Phosphate=
Pyrolysis
dioxide released
acetic acid vapors
Combustion
released T=TATM T<200 oC
Key
= Cloisite = Phosphate
6 Browne, F.L. Theories of the Combustion of Wood and Its Control. A Survey of the
T=200 oC T<280 oC
Pyrolysis
reactions continue
diffusing
Combustion
reached (~240 oC)
within the wood
Pyrolysis
smoke
T~400 oC
Combustion
vapor combustion
around T=400 oC T=280 oC T<500 oC
Pyrolysis
reached
complete carbonization process
are further pyrolyzed into more combustible products T>500 oC
Combustion
resulting from exothermic rxns.
consumed
cease
remains
gained from consuming a good or a service
enhance a products’ appeal (demand) to the consumer
maximum happiness
attempts to maximize utility (happiness)
Utility Curve
10 20 30 40 50 60 70 80 90 100 1 2 3 4 5 6 7 8 9 10
Number of Drinks C
er Satisfaction
Utility Curve
10 20 30 40 50 60 70 80 90 100 1 2 3 4 5 6 7 8 9 10
Number of Drinks Consumer Satisfaction
Maximum consumer satisfaction
Ex: Let 1-scoop of ice cream 50% happy (0.50) 2-scoops of ice cream 75% happy (0.75)
physical property
Ex: Measure, 1-scoop = 0.50 wt% sucrose (C12H22O11) 2-scoop = 1.00 wt% sucrose (C12H22O11)
amount in each “scoop”
from changes in sugar concentrations
Retardancy Time
10 20 30 40 50 60 70 80 90 100 20 40 60 80 100 120 140 160 180 200 Time (sec) % H a ppine ssThickness
10 20 30 40 50 60 70 80 90 100 1 2 3 4 5 6 7 8 # Applications % HappinessOdor
10 20 30 40 50 60 70 80 90 100 1 2 3 4 5 6 7 8 9 10 Odor (unitless) % Happiness
Setting Time
10 20 30 40 50 60 70 80 90 100
50 100 150 200 250 300
Setting Time (min) % Happiness
comparison
product
Effective % Coated
10 20 30 40 50 60 70 80 90 100 10 20 30 40 50 60 70 80 90 100 % Coated % Happiness
consumer attributes
based on their relative importance
i i i i
th i =
th i
1 2
0.04
Toxicity
0.04
Biodegradability
0.07
Effective amount
0.25
Setting time
0.15
Odor
0.15
Thickness
0.30
Retardancy time
Weight Consumer Attribute
product and a “happy” product
thickness (Basis 10cm X 10cm X 2cm)
@ ~ 1mm/coat)
source
barrier degrades inducing char on wood
increase
gasses
emitted
formatoin
Heat Released Time Fast Pyrolysis Slow Pyrolysis
6 Browne, F.L. Theories of the Combustion of Wood and Its Control. A Survey of the
Char Formation6
char i i i i
m m m m X − − =
, ,
mi=Mass ith component initially, (0,i), after heating, (i), (kg) mchar=Mass of char developed (kg)
Char Layer Kinetics6
n i RT E i i
X e A dt dX
avg A
− =
−
1
Ai=Frequency factor (min-1) EA=Activation Energy (kJ/mol) R=Gas constant (kJ/mol-K) Tavg=Average wood temperature (K) n=Reaction order (unitless)
6 Browne, F.L. Theories of the Combustion of Wood and Its Control. A Survey of the
Char Layer Kinetics (cont’d)
H H T L L T C C T W T
avg avg avg avg
WW=Wood as a whole WC =Cellulose component WL=Lignin component WH=Hemicellulose component
number of applications
1
x x n =
1
x k D m
c AB
=
A As A As
C C C C Y − − =
2 1
x t D X
AB
=
112 . ) ln( 392 . + − = Y X
7Welty, et al. Fundamentals of Momentum, Heat & Mass Transfer. 4th Edition.
John Wiley & Sons, Inc 2001.
average thickness (~1mm)
Hydrocar
1
Alcohols/ halogens
2
Carboxylic Acids
3
Ethers
4
Aromatics
5
Amines
6
Ketones
# F.G.
7
Mercaptans
percentage ~ 35% by volume)
happiness
most profitable product
happiest product
H1=0.868 H2=0.574
661 .
1 2 =
= H H β
H1=0.930 H2=0.574
617 .
1 2 =
= H H β
Tank 1 Tank 2 Storage Tank Pump 1 Pump 2 L/L Sep. Evaporator Extruder Conveyor PVAc NaOH/H2O NaAc Cloisite Phosphate
to each other will give our demand
=
β α
α β
2 1 2 2 1 1
d d d p d p
2 2 1 1
d p d p Y + =
β α
β α
−
− =
1 2 1 1 2 1 2 1 1
p d p p Y p p d d
6,700,000 10 6,300,000 9 6,000,000 8 5,800,000 7 5,500,000 6 5,300,000 5 4,900,000 4 3,900,000 3 930,000 2 19,000 1 Demand (lb/year) Year
Year 4 1,000,000 2,000,000 3,000,000 4,000,000 5,000,000 6,000,000 7,000,000 8,000,000 9,000,000 1,000,000 2,000,000 3,000,000 4,000,000 5,000,000 6,000,000 d1 p h i (d 1)$ 9,000,000 $15,000,000 $22,000,000 Max $ 9,000,000 $15,000,000 $22,000,000 Design 3 $ 6,000,000 $13,000,000 $19,000,000 Design 2 $ (6,100,000) $ (1,300,000) $ 3,600,000 Design 1 High Med Low NPW
Minimax Design 3 3,000,000 3,000,000 2,000,000 3,000,000 Design 2 18,400,000 15,100,000 16,300,000 18,400,000 Design 1 Max Regret High Med Low Regret
85 m3 Storage 0.7 m3 Extruder 3.2 m3 Evaporator 6.8 m3 Settler 0.6 kW Pump 2 4.9 kW Pump 1 4.1 m3 Tank 2 7.2 m3 Tank 1
Capacity Component
$16,000 Heater 1 $25,000 Dryer $76,000 Settler $5,000 Pump 2 $7,000 Pump 1 $25,000 Tank 2 $40,000 Tank 1 $310,000 Total Cost $5,000 Piping $40,000 Storage $18,000 Conveyor $47,000 Extruder $6,000 Heater 2
$(20,000,000) $(10,000,000) $- $10,000,000 $20,000,000 $30,000,000 $40,000,000 $50,000,000 2006 2007 2008 2009 2010 2011 2012 2013 2014 2015 2016 Cash Flow Cash Balance
TCI i SV WC i CF NPW
n n n
− + + + + =∑
= 10 10 1
) 1 ( ) 1 (
8West, et al. Plant Design and Economics for Chemical Engineers. 5th Edition.
McGraw-Hill 2004.
Distribution for Design 3 NPW
0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8 2 6 12 18 24
Values in Millions Values in 10^ -7
markets in Houston, Dallas, Kansas City
1. How Flame Retardants Work? EFRA. Accessed January 2006. <http://www.cefic-efra.com/> 2. United States Fire Administration. National Fire Statistics. Accessed January 2006. www.usfa.fema.gov/statistic/national/ 3. Lerner, Ivan. “FR Market Down but Not Out: Albemarle Stays the Course.” Chemical Market Reporter. December 10, 2001 p. 12. 4. Mazali, C.A.I. and M.I. Felisberti. Vinyl Ester Resin Modified with Silicone-Based Additives:II. Flammability Properties. www.interscience.wiley.com. Accessed April 2006. 5. Hussain, M., et.al. Effect of Organo-Phosphorus and Nano-Clay Materials on the Thermal and Fire Performance of Epoxy Resins. Journal of Applied Polymer Science, Vol. 91,1233-1253. 2003 6. Browne, F.L. Theories of the Combustion of Wood and Its Control. A Survey of the Literature. Forest Products Laboratory, Forest Service U.S. Department of Agriculture. 7. Welty, et al. Fundamentals of Momentum, Heat & Mass Transfer. 4th Edition. John Wiley & Sons, Inc 2001. 8. West, et al. Plant Design and Economics for Chemical Engineers. 5th Edition. McGraw-Hill 2004.