2. CEO – CHRISTINE OBEK
COO – CHLOE NEOH
CFO – JASON TIONG
ASST. COO – FARAH AMELIA
PR OFFICER – DANIEL PHUAN

5. Summary of Feedstocks to be co-gasified
PALM OIL BIOMASS
HDPE WASTE
Amounts to 85.5% of total biomass production in Malaysia
Amounts to 60.1% of total plastic waste produced in Malaysia
High potential for producing renewable energy (98.7%)
Capable of producing high concentrations of hydrogen gas
Over palm oil 400 mills in Malaysia

6. PASIR GUDANG, JOHOR BAHRU
Comparison of available choices for Plant location
FACTORS
SAMALAJU, BINTULU
PASIR GUDANG, JOHOR BAHRU
LAHAD DATU, SABAH
Land Cost
(USD 000’)
10.4
253.5
284.3
Electricity Cost (USD/kWh)
0.06
0.10
0.08
Special Features
Water treatment plant located in Samalaju.
Nil

9. MEMBRANE SEPARATOR FIXED BED FLUIDIZED BED GASIFIER GASIFIER SCRUBBER
WATER
STEAM
FEED (BIOMASS + PLASTIC)
ASH
FLUIDIZED BED PRODUCT GAS
FIXED BED PRODUCT GAS
TAR + WATER
TAR
SCRUBBED GAS
ENRICHED SYNGAS
ENRICHED HYDROGEN
CARBON DIOXIDE GAS
MEMBRANE
SEPARATOR
FIXED BED
GASIFIER
FLUIDIZED BED
GASIFIER
SCRUBBER
ADIABATIC
REACTOR
LEGEND:
R – 101 A = FLUIDIZED BED GASIFIER
R – 102 A = FIXED BED GASIFIER
V – 101 A = SCRUBBER
R – 103 A = ADIABATIC REACTOR
R – 105 A = MEMBRANE SEPARATOR
R – 104 A = SETTLING TANK
B – 101 = SCREW CONVEYER BELT
T – 101 = WATER TANK
E – 101 A = STEAM GENERATOR
E – 102 A = COOLER
E – 103 A = COOLER
M – 101 A = MIXER
K – 101 = COLLECTOR
P – 101 A = PUMP
P – 102 A = PUMP
VLV – 101 A = THREE WAY VALVE
VLV – 102 A = VALVE
VLV – 103 A = VALVE
VLV – 104 A = VALVE
VLV – 105 A = VALVE

10. LEGEND:
R – 101 A = FLUIDIZED BED GASIFIER
R – 102 A = FIXED BED GASIFIER
V – 101 A = SCRUBBER
R – 103 A = ADIABATIC REACTOR
R – 105 A = MEMBRANE SEPARATOR
R – 104 A = SETTLING TANK
B – 101 = SCREW CONVEYER BELT
T – 101 = WATER TANK
E – 101 A = STEAM GENERATOR
E – 102 A = COOLER
E – 103 A = COOLER
M – 101 A = MIXER
K – 101 = COLLECTOR
P – 101 A = PUMP
P – 102 A = PUMP
VLV – 101 A = THREE WAY VALVE
VLV – 102 A = VALVE
VLV – 103 A = VALVE
VLV – 104 A = VALVE
VLV – 105 A = VALVE

11. Price of Feedstock and Hydrogen in 3 different scenarios
BEST
BASE
WORST
FEEDSTOCK
($ millions/KG)
0.04
0.64
1.12
HYDROGEN
823
764
707
BEST
BASE
WORST
FEEDSTOCK ($/KG)
0.04
0.06
0.11
HYDROGEN ($/KG)
8.23
7.64
7.07
FEED SUPPLY OF 1,000,000 KG/YEAR
PRODUCTION RATE OF 100,000,000 KG/YEAR

12. OPERATIONAL LIFE :20 YEARS
Operating Cost + Fixed Charges
Total Hydrogen Production price – sales - TPC
BEST
BASE
WORST
SALES TAX ($millions)
4.12
3.82
3.54
TOTAL PRODUCT COST ($millions)
56.2
56.8
57.3
REVENUE ($millions)
22.0
15.8
9.91
NET PROFIT BEFORE TAXES ($millions)
23.4
16.8
10.7
OPERATIONAL LIFE :20 YEARS
20%
25%
BEST
BASE
WORST
TOTAL TAX PAID ($millions)
110
67.2
53.4
NET PROFIT AFTER TAX ($millions)
357
268
160

13. Returns of Investment (ROI)
Payback Period
BEST
4.56 YEARS
BASE
4.81 YEARS
WORST
6.92 YEARS
PAYBACK PERIOD
Returns of Investment (ROI)
Best
Base
Worst
BEST
BASE
WORST
PRE-TAX (%)
28.4
20.46
11.6
AFTER-TAX (%)
21.7
16.4
5.7