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Biodiesel Production, Usage and Government Policy in Thailand
By Mr. Sanin Triyanond Chairman, Thai Biodiesel Producer Association
Director, Patum Vegetable Oil Co.,Ltd
Biodiesel History in Thailand
Government Policy
Technical Background
Biodiesel Production & Usage
Conclusion
Contents
Biodiesel History in Thailand
2005 2007 2010 2011 2014 Conventional Diesel
+ B5
B2 , B5
B3, B5
B5
B7
- In 1985, royal initiative project related biodiesel has been firstly established.
- In 2005, biodiesel has been officially implemented across the country.
- In 2008, Thai government has initially established Renewable Energy Development Plan to promote the use of alternative energy
Government Policy
Biodiesel Mandate Worldwide
Thailand : B7
Taiwan : B2
South Korea : B2
Australia : B2
Indonesia : B10
Malaysia : B5
Philippines : B2
Brazil : B5
Canada : B2
Argentina : B10
Peru : B2
Ecuador : B5
Costa Rica : B20
Paraguay : B1
EU : 10% of Renewable Energy in all transport
fuel in 2020
Source : Biofuel Mandate Around the World: 2014, http://globalrfa.org Note: Information on this slide may not be up-to-date
Goal : Committed to the development of low-carbon society
AE
Solar &
Wind
Hydro Power Plant
Bio
energy New
Energy
Biofuel
Alternative Energy Development Plan (AEDP) 2012-2021
Source: Department of Alternative Energy Development and Efficient
Target : 25% of AE in total energy consumption by 2021
AEDP 2012-2021
Biofuel
Ethanol
Biodiesel New Fuel for Diesel Substitute
9 ML/D
3 ML/D
Source: Department of Alternative Energy Development and Efficient
7.2 ML/D
Supply
• Support palm plantation area of 5.5 million rai & get a total palm yielding of 5.3 million rai • Increase CPO production capacity to > 3.05 mt/yr. • Increase oil palm yielding to > 3.2 T/Rai/Y & oil content 18%
Demand • Manage blending ratio according to domestic CPO production • Pilot project of using B10 or B20 in fleet trucks or proper fishery boats • Develop FAME standard to 7% blending ratio in diesel
Biodiesel 7.2 ML/D
AEDP 2012-2021
Biofuel
Ethanol
Biodiesel New Fuel for Diesel Substitute
9 ML/D
3 ML/D
Source: Department of Alternative Energy Development and Efficient
7.2 ML/D
New Energy Feedstock Development (Jatropha, Algae)
Use of ethanol for blending to substitute diesel (FAEE, ED95, Diesohol)
Development of oil conversion technology (BHD, BTL)
New Fuel for Diesel Substitute
3 ML/D
algae oil palm Targeted Feedstock for FAME and BHD Targeted Feedstock for BTL
2013 2014 2017 2021
FAME 2.9 ML/D FAME ~3.4 ML/D FAME ~4.2 ML/D
BHD ~2.0 ML/D
FAME 7.2 ML/D
NFDS 3 ML/D
AEDP 2012-2021
Technical Background
World Feedstock
catalyst
CH2-O-C-R
O
CH -O-C-R
O
CH2-O-C-R
O 3R’-O-C-R
O
R’- OH
Tri-glycerol (Vegetable Oil)
Alcohol Alkyl ester (Biodiesel)
+
CH2-OH
CH -OH
CH2-OH
Glycerol
+
Transesterification reaction
Parameter Unit Spec Purity % wt. 96.5 min Density @ 15 ºC kg/m3 860-900 Kinematic Viscosity@ 40 ºC mm2/s 3.5-5.0 Flash Point, (P.M.) ºC 120 min Sulphur Content mg/kg 10.0 max Carbon Residue % wt. 0.30 max Cetane Number - 51 min Sulphated Ash % wt. 0.02 max Water Content mg/kg 500 max Total Contaminate mg/kg 24 max Copper Strip Corrosion - No.1 max Oxidation stability @ 110 ºC hr 10 min Acid Value mg KOH/g 0.5 max Iodine Value g l2/100 g 120 max
Parameter Unit Spec Linolenic Acid Methyl Ester % wt. 12.0 max Methanol % wt. 0.2 max Monoglyceride % wt. 0.70 max Diglyceride % wt. 0.20 max Triglyceride % wt. 0.20 max Free Glycerin % wt. 0.20 max Total Glycerin % wt. 0.25 max Phosphorus mg/kg 10 max Group 1 Metals (Na + K) mg/kg 5.0 max
Group 2 Metals (Ca + Mg) mg/kg 5.0 max
Cloud Point ºC Report CFPP ºC Report Additives - Approval
Thai Biodiesel Specification
Parameter Unit Spec Purity % wt. 96.5 min Density @ 15 ºC kg/m3 860-900 Kinematic Viscosity@ 40 ºC mm2/s 3.5-5.0 Flash Point, (P.M.) ºC 120 min Sulphur Content mg/kg 10.0 max Carbon Residue % wt. 0.30 max Cetane Number - 51 min Sulphated Ash % wt. 0.02 max Water Content mg/kg 500 max Total Contaminate mg/kg 24 max Copper Strip Corrosion - No.1 max Oxidation stability @ 110 ºC hr 10 min Acid Value mg KOH/g 0.5 max Iodine Value g l2/100 g 120 max
Parameter Unit Spec Linolenic Acid Methyl Ester % wt. 12.0 max Methanol % wt. 0.2 max Monoglyceride % wt. 0.70 max Diglyceride % wt. 0.20 max Triglyceride % wt. 0.20 max Free Glycerin % wt. 0.20 max Total Glycerin % wt. 0.25 max Phosphorus mg/kg 10 max Group 1 Metals (Na + K) mg/kg 5.0 max
Group 2 Metals (Ca + Mg) mg/kg 5.0 max
Cloud Point ºC Report CFPP ºC Report Additives - Approval
Thai Biodiesel Specification
Feedstock C8:0 C10:0 C12:0 C14:0 C16:0 C18:0 C18:1 C18:2 C18:3
4.6- 10.0
5.0-8.0 45.1-53.2
16.8-21 7.5-10.2
2.0-4.0 5.0-10.0 1.0-2.5 ND-0.2
ND ND ND – 0.5
0.5 – 2.0
39.3-47.5
3.5-6.0 36.0-44.0
9.0-12.0 ND-0.5
ND ND ND ND-0.2 2.5-7.0
0.8-3.0 51.0-70.0
15.0-30.0
5.0-14.0
ND ND ND-0.1 ND-0.2 8.0-13.5
2.0-5.4 17-30 48.0-59.0
4.5-11.0
ND ND ND-0.1 ND-0.2 5.0-7.6
2.7-6.5 14.0-39.4
48.3-74.0
ND-0.3
ND- non detectable, defined as < 0.05% Fatty Acid Composition (%)
Source: Codex Stan 210-1999
Feedstock Cetane number Cloud point (°C) CFPP (°C) Iodine value Oxidation stability (hr)
61.0 (6.46) -1.2 (3.9) -4.7 (0.6) 7.8 (2.5) 11.0 (5.64)
61.2 (4.90) 13.3 (2.3) 11.4 (4.7) 52.7 (5.6) 11.4 (2.38)
54.1 (3.32) -3.3 (2.4) -11.3 (5.9) 111.7 (7.4) 7.4 (1.81)
51.8 (3.93) 0.1 (2.0) -3.6 (3.4) 126.0 (6.9) 5.0 (2.59)
51.9 (4.73) 0.9 (2.4) -3.5 (2.0) 128.6 (2.1) 1.3 (0.42)
Biodiesel Properties *(Standard deviation in parentheses)
Source: A Statistical investigation of biodiesel physical & chemical properties, and their correlation with the degree of unsaturation, published in “Renewable Energy”, Vol.50, 2013
Biodiesel Production & Usage
0
50,000
100,000
150,000
200,000
250,000
Jan
-10
Mar
-10
May
-10
Jul-
10
Sep
-10
No
v-1
0
Jan
-11
Mar
-11
May
-11
Jul-
11
Sep
-11
No
v-1
1
Jan
-12
Mar
-12
May
-12
Jul-
12
Sep
-12
No
v-1
2
Jan
-13
Mar
-13
May
-13
Jul-
13
Sep
-13
No
v-1
3
Jan
-14
Mar
-14
Quantity (T/M)
CPO Production vs Demand, Jan 2010 – Mar 2014
Edible Oil & Other Industries
Export / Biodiesel
Source: Department of Internal Trade
40.0
45.0
50.0
55.0
60.0
Jan
-10
Mar
-10
May
-10
Jul-
10
Sep
-10
No
v-1
0
Jan
-11
Mar
-11
May
-11
Jul-
11
Sep
-11
No
v-1
1
Jan
-12
Mar
-12
May
-12
Jul-
12
Sep
-12
No
v-1
2
Jan
-13
Mar
-13
May
-13
Jul-
13
Sep
-13
No
v-1
3
Jan
-14
Mar
-14
Vol (ML/D)
HSD Consumption, Jan’10 – Mar’14
49.6 ML/D 51.4 ML/D 54.7 ML/D 55.9 ML/D
Source: Department of Energy Business
0.0
1.0
2.0
3.0
4.0
Jan
-10
Mar
-10
May
-10
Jul-
10
Sep
-10
No
v-1
0
Jan
-11
Mar
-11
May
-11
Jul-
11
Sep
-11
No
v-1
1
Jan
-12
Mar
-12
May
-12
Jul-
12
Sep
-12
No
v-1
2
Jan
-13
Mar
-13
May
-13
Jul-
13
Sep
-13
No
v-1
3
Jan
-14
Mar
-14
Vol. (ML/D)
B2
B5 B4 B3
B7
B100 Consumption and Blending Ratio, Jan’10 – Mar’14
1.6 ML/D 1.7 ML/D 2.4 ML/D 2.9 ML/D
1,400,000
800,000
685,800
500,000
300,000
300,000
300,000 220,000
200,000 200,000 50,000
(1) Patum Vegetable Oil
(2) Energy Absolute
(3) Thai Oleochemical
(4) AI Energy
(5) Bangchak Biofuel
(6) Absolute Power P
(7) Pure Biodiesel
(8) New Biodiesel
(9) B. Grimm Greenpower
(10) Verasuwan
(11) Bangchak Petroleum
(2) (3)
(4)
(5)
(6)
(7)
Source : Department Of Energy Business , Feb 2014
20
30
40
50
60
70
2011 2012 2013 2014
(1) (8) (9) (10) (11)
Unit : ML/D
Current B100 Producers and Production Capacity
Total Cap : ~ 5 ML/D
Total Plant Utilization (%)
Conclusion
• Biodiesel has been around for years.
• Government has and will push biodiesel policy consistently.
• Solid development plan (AEDP) has been set.
• Biodiesel is globally adopted, but maximum blending ratio remains unrevealed.
• Various feedstock gives different biodiesel properties.
• Palm oil is currently major feedstock.
• CPO production and diesel/biodiesel consumption are growing.
• “Sustainability” cannot come from one party.