A Review on Prospect of Jatropha Curcas for Biodiesel in Indonesia
Cleaning Agent Utilization for Jatropha (Jatropha curcas) Biodiesel Purification
Transcript of Cleaning Agent Utilization for Jatropha (Jatropha curcas) Biodiesel Purification
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8/14/2019 Cleaning Agent Utilization for Jatropha (Jatropha curcas) Biodiesel Purification
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LEMBAGA PENGEMBANGAN DAN PEMBERDAYAAN MASYARAKAT
INSTITUT PERTANIAN BOGORBOGOR
2008
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WHAT IS BIODIESEL??Biodiesel is an alternative fuel aside frompetroleum based fuel we have knownbefore.
Biodiesel is categorized as biofuelbecause of its renewable characteristic.
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Jatropha oil
Esterification,temperature 55 0C, 1 hour
Transesterification,temperature 55 0C, 1 hour
H2SO
4+
Methanol
KOH +Methanol
Precipitation and biodieselseparation from water andglycerol
Precipitation and separation from water and methanol residues
Crudebiodiesel
Glyceroland water
Methanolresidues
and water
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Biodiesel purification
IMPORTANT!!
Crude biodiesel contain impurities
Performances Machines
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Biodiesel Purification Methods
Dry washing VS Wet washing
Cleaning agent Water
PROSPECTIVE ALTERNATIVE
WHY??
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Differences between wet washing and drywashing
Wet washing Dry washingMore investment needed Less investment needed
More energy needed Less energy neededMore drying time needed No needs for drying time
Less quality of biodiesel that
have been produced
Better quality of biodiesel that
have been produced
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Cleaning Agent Preparation
Cleaning agent Low Adsorption
ACTIVATIONActivation of cleaning agent is aimed to enlarge
the contact surfaces of adsorbent throughpores structure forming that increase itsadsorption.
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Activation MethodTheres 2 method, e.g.
Drying
Acid-base activation using HCl or H 2SO4
Based on Diaz and Santos (2001), acid-baseactivation shows significant differences of physic-chemical characteristic such as surfaces and poresvolumes between activated clay and non-activated one.
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Acid-base Activation Reaction in
Cleaning AgentBased on Ketaren (1986), reaction that happened whenacid-base activation applied on cleaning agent are
First, the acid dissolve Al 2O3,CaO, and MgO that fill inadsorbents pores so the pores will be widely openedand the contact surfaces enlargedCa++ dan Mg ++ ions are substituted by H + ions from the
mineral acidSome of H + ions that substitute Ca ++ dan Mg++ will bereplaced by Al +++ ions within acid aqueous liquid
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Cleaning Agent ActivationB/T 100-200 g
Warming and agitation ontemperature
80 oC for 3 hours
Activated cleaningagent
Washing wastewater
HClseparation
Washing for5 times until pH 3,5-4,0
Drying on temperature110 oC for 2 hours
Aquadest
400 ml HCl 16 %
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Cleaning agentagitation using HCl,temperature 80 oC, 3
hours
Cleaning agentagitation after 3
hours
Cleaning agent and HClseparation using vacuum
filter
Cleaning agentwashing by water
Waste water and cleaningagent separation using
vacuum filter
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Biodiesel Purification by Cleaning
AgentCrude biodiesel
Agitation, constant speed,20 minutes, room temperature
Cleaning Agent
Precipitation,for 2-3 hours
Filtering
Pure Biodiesel
Adsorbentsresidues
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Cleaning agent s weightmeasuring
Mixing cleaning agentwith biodiesel
Agitation at 20 minuteslong
Precipitation for 2 hourslong
Separation betweencleaning agent and
biodiesel
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Biodiesel Analysis
Parameters which used for analyzingeffectiveness of biodiesel purification process
by cleaning agent are acid value soap and catalyst value glycerol value (free, bound, and total)
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Acid Value Graphic
0.000.10
0.20
0.30
0.40
0.50
0.60
0.70
0.80
0.90
B i l a n g a n A s a m
( m g K O H
/ g b i o
d i e s e
l )
Jenis Perlakuan Pemurnian
Bil Asam (mgKOH/gbiodiesel)Standar
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Lowest acid value measured
T100% = 0,1467 mg KOH/g biodiesel
Comparison
Water-washing biodiesel = 0,2341 mg KOH/g biodiesel
Biosponge = 0,2155 mg KOH/g biodieselStandard = 0,8000 mg KOH/g biodiesel
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Soap Value Graphic
0.00
500.00
1000.00
1500.00
2000.00
2500.00
3000.00
3500.00
K a
d a r S a
b u n
( p p m
)
Jenis Perlakuan Pemurnian
Kadar Sabun(ppm)
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Catalyst value undetected
Lowest soap value measured
B100% = 53,37 ppm
Comparison
Water-washing biodiesel = 17,79Biosponge = 22,23
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Free Glycerol Value Graphic
0.00
0.01
0.01
0.02
0.02
0.03
0.03
0.04
0.04
K a
d a r G
l i s e r o
l B e b a s
( % - b
e r a t )
Jenis Perlakuan Pemurnian
Gbbs %-b
Standar
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Lowest free glycerol value measured
B = 0,0054 %-weight
Comparison
Water-washing biodiesel = 0,0014 %-weight
Biosponge = 0,0184 %-weightStandard = 0,0200 %-weight
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Bound Glycerol Value Graphic
0.0000
0.0500
0.1000
0.1500
0.2000
0.2500
0.3000
K a
d a r G
l i s e r o
l T e r i
k a t
( % - b
e r a t )
Jenis Perlakuan Pemurnian
Gikt %-b
Standar
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Lowest bound glycerol value measured
B : T (2 : 1) = 0,2190 %-weight
Comparison
Water-washing biodiesel = 0,2575 %-weight
Biosponge = 0,2229 %-weightStandard = 0,2200 %-weight
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Total Glycerol Value Graphic
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0.05
0.1
0.15
0.2
0.25
0.3
0.35
K a
d a r G
l i s e r o
l T o t a
l ( % - b
e r a t )
Jenis Perlakuan Pemurnian
Gttl %-b
Standar
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Lowest total glycerol value measured
B : T (2 : 1) = 0,2318 %-weight
Comparison
Water-washing biodiesel = 0,2589 %-weight
Biosponge = 0,2413 %-weightStandard = 0,2400 %-weight
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Best Cleaning Agent
B 100% and B : T (2 : 1)
Water Content Analyzing
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Water Content
0
0.02
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0.1
0.12
BCA Biosponge B100% B2T1
K a
d a r A i r ( %
)
Jenis Perlakuan Pemurnian
Kadar Air (ml/100 mlBiodiesel)
Standar
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Lowest Water Content Measured
B 100% = 0,01 %
Comparison
Water-washing biodiesel = undetected
Biosponge = undetectedStandard = 0,05 %
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Conclusion Cleaning agent utilization can be applied as analternative for purificating biodiesel, becausecleaning agent effectively reduce impurities from
crude biodiesel and efficiently less investment. This can be viewed from significant decreasing of acid value, soap value, and free glycerol value fromcleaning-agent-purificated biodiesel.