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

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

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

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

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

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

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

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