Official Journal of the Japan Wood Research Society
Stage | Process | Numerical value | Unit | Note | ||
---|---|---|---|---|---|---|
Raw material procurement | Wood powder production | Input | Fine grinding | 2.94E+00 | kg | By-product wood is turned into wood powder |
Transportation (wood powder) | Input | Outward route | 2.94E−01 | tkm | Assumes procurement from within the same prefecture | |
Transportation (wood powder) | Input | Return route | 9.87E−02 | km | ||
PEG production | Input | 1.95E−01 | kg | |||
Transportation (PEG) | Input | Outward only | 2.57E−01 | tkm | Assumes maximum domestic transport distance | |
H2SO4 production | Input | 8.53E−02 | kg | |||
Transportation (H2SO4) | Input | Outward only | 6.80E−02 | tkm | H2SO4 (62% W.B) Assumes maximum domestic transport distance | |
NaOH Production | Input | 1.66E−01 | kg | |||
Transportation (NaOH) | Input | Outward only | 1.71E−01 | tkm | NaOH (48.5% W.B.) Assumes maximum domestic transport distance | |
Production | Reaction | Input | Recycled chemical agents | 4.79E+00 | kg | PEG 73.4%, Other residues 26.6% |
Input | Electricity | 3.93E−01 | kWh | |||
Input | Natural gas | 1.33E−01 | m3 | |||
Input | Industrial water | 5.06E+00 | kg | |||
Output | Mixed solution A | 2.91E+01 | kg | |||
Output | Drainage | 3.33E−04 | m3 | |||
Solid–liquid separation | Input | Mixed solution A | 2.91E+01 | kg | ||
Input | Electricity | 8.47E−02 | kWh | |||
Output | Mixed solution B | 2.59E+01 | kg | |||
Output | Pulp | 3.17E+00 | kg | Pulp 48.4%, Water 35.7%, PEG13.8%, etc | ||
pH adjustment | Input | Mixed solution B | 2.59E+01 | kg | ||
Input | H2SO4 (62% W.B) | 2.08E−01 | kg | |||
Input | Industrial water | 7.86E−01 | kg | |||
Input | Electricity | 8.85E−02 | kWh | |||
Output | Mixed solution C | 2.69E+01 | kg | |||
Washing and filtration | Input | Mixed solution C | 2.69E+01 | kg | ||
Input | Electricity | 4.37E−01 | kWh | |||
Input | H2SO4 (62% W.B) | 2.88E−01 | kg | |||
Input | Industrial water | 3.53E+01 | kg | |||
Output | PEG-modified lignin (61.5% W.B) | 2.47E+00 | kg | |||
Output | Supernatant | 2.39E+01 | kg | To the reclamation process | ||
Output | Drainage | 3.60E−02 | m3 | Includes saccharides and PEG-modified lignin residue | ||
Drying | Input | PEG-modified lignin (61.5% W.B) | 2.47E+00 | kg | PEG-modified lignin 36%, Saccharides 2.4% | |
Input | Electricity | 1.23E−01 | kWh | |||
Output | PEG-modified lignin (5% W.B) | 1.00E+00 | kg | |||
Reprocessing | Input | Supernatant | 2.39E+01 | kg | ||
Input | NaOH (48.5% W.B) | 3.27E−01 | kg | |||
Input | Electricity | 4.94E−02 | kWh | |||
Output | Recycled chemical agents | 4.79E+00 | kg | PEG 73.4%, Other residues 26.6% | ||
Output | By-product salt | 1.75E+00 | kg | |||
Output | Drainage | 1.84E−02 | m3 |