Materiały konferencyjne SEP 2018

Przykład 2: LCA procesu produkcji REE ze źródeł wtórnych 0,16 kg Chemical, organic {GLO}| market for | 12,4 % 0,16 kg Chemical, organic {GLO}| production | 12,3 % 0,0413 kg Coconut oil, crude {GLO}| market for | 9,77 % 1,38 MJ Electricity, high voltage {SE}| heat 8,08 % 22,2 MJ Electricity, high voltage {SE}| 13,5 % 0,16 kg Fatty acid {GLO}| market for | Alloc 27,3 % 0,0529 kg Fatty acid {RER}| production, from 8,89 % 0,107 kg Fatty acid {RoW}| production, from 18,2 % 2,08 MJ Heat, district or industrial, other 6,56 % 990 kg Non-sulfidic tailing, off-site 116 % 0,339 kg Palm fruit bunch {GLO}| market for | 10,4 % 0,0413 kg Palm kernel oil, crude {GLO}| market 5,85 % 0,0233 kg Palm kernel oil, crude {RoW}| palm 3,3 % 0,7 kg Sodium silicate, solid {GLO}| market 16,6 % 0,469 kg Sodium silicate, solid {RoW}| 10,7 % 2,1 MJ Heat, district or industrial, other 6,59 % 0,339 kg Wood chips, wet, measured as dry 8,01 % 1E3 kg New Kankberg gold tailings -86,9 % 10 kg REE Concentrate production, New 100 %