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%