Umpan/Bahan Tambahan Patent A WO 201800574 Production of Propionaldehyde Metana Syngas (H2 and CO) Oksigen Air (H2O) BscHons Marina Hop Production of Propionaldehyde n-propanol Nitrogen Hydrogen Air (H2O) Patent B US3862236 Production of Propionaldehyde Alil Alohol - Gliserol Air (H2O) Sodium sulfat H2 Akrolein Tubular Reactor Fixed Bed Reactor Fixed Bed Reactor 100-200 oC 250 oC Tekanan steam tinggi WO3 Tungsten trioxide 180 oC WO3 Tungsten trioxide Dehidrasi hidrogenasi Laura Malek Production of Propionaldehyde KondisiOperasi 2. T Reaktor1 750-1000 oC Multitubular Reactor 220-320 oC 3. P Reaktor 1 100-500 kPa 81,1- 101,3 kPa 4. T Reaktor 2 5. P Reaktor 2 280-340oC 100-10000 kPa Catalyst SiO2/NiS 1. Jenis Reaktor Jenis Reaksi Alat penunjang Conversi Multitubular Reactor OCM Reaction, Water Shift Gas Reaction Distilation Column Partial Condenser Boiler Propionaldehyde 98% ± 10 atm gauge - Copper Chromite Metallic Paladium Dehidrogenation 100 atm Preheater Condenser Rotameter Flask Kondenser Cooler Distilation Column Evaporator Distilation Column Propionaldehyde 63% Propionaldehyde 96.5% Propionaldehyde 99.5% Propionaldehyde 99.5%