Table 4.
Comparison and evaluation of all routes and sub‐routes based on atom economy, RME, sustainability based on green chemistry principles, and maturity.
|
Primary pathway |
Process step |
Atom economy[a] [%] |
RME[b] [%] |
Sustainability[c] (1–5) |
Maturity[d] |
|---|---|---|---|---|---|
|
direct conversion of CO2 |
classic electrochemistry |
152 |
137 |
3.50 |
bench |
|
metal‐complex electrochemistry |
152 |
146 |
3.65 |
lab |
|
|
sacrificial ascorbate reduction |
61 |
49 |
3.93 |
lab |
|
|
formate coupling |
carbonate reduction |
79 |
78 |
4.21 |
bench |
|
photochemical reduction |
73 |
69 |
4.21 |
pilot |
|
|
photochemical reduction |
73 |
47 |
3.87 |
bench |
|
|
enzymatic production |
– |
– |
4.14 |
bench |
|
|
caustic CO reduction |
100 |
97 |
3.93 |
commercial |
|
|
formate coupling |
99 |
98 |
4.36 |
commercial |
|
|
CO to oxalic acid |
Boudouard reaction |
100 |
80 |
2.00 |
commercial |
|
coal gasification |
33 |
8 |
3.29 |
commercial |
|
|
steam reforming |
93 |
75 |
1.86 |
commercial |
|
|
partial oxidation |
92 |
74 |
2.21 |
commercial |
|
|
biomass gasification |
X |
X |
4.14 |
pilot |
|
|
reverse water‐gas shift |
61 |
33 |
4.14 |
commercial |
|
|
electrochemical reduction |
61 |
52 |
4.07 |
bench |
|
|
photochemical reduction |
61 |
61 |
4.14 |
lab |
|
|
electrolysis (solid oxide electrolyzer cell) |
64 |
51 |
4.14 |
commercial |
|
|
dialkyl oxalate process |
98 |
96 |
3.00 |
commercial |
|
|
direct biomass conversion |
alkali fusion |
27 |
22 |
2.79 |
commercial |
|
oxidation |
92 |
60 |
3.79 |
commercial |
|
|
fermentation |
X |
X |
3.86 |
bench |
|
|
EG oxidation |
ethylene oxide hydrolysis |
100 |
90 |
1.96 |
commercial |
|
glycerol oxidation |
69 |
59 |
3.93 |
pilot |
|
|
catalytic EG oxidation |
71 |
67 |
3.71 |
commercial |
|
|
electrochemical EG oxidation |
71 |
67 |
4.22 |
bench |
|
|
propylene oxidation |
steam cracking |
90 |
90 |
1.93 |
commercial |
|
fossil on‐purpose processes |
X |
X |
1.85 |
commercial |
|
|
bioethanol dehydrogenation |
53 |
48 |
3.14 |
pilot |
|
|
Fischer‐Tropsch to olefins |
67 |
64 |
3.12 |
lab |
|
|
direct hydrogenation |
36 |
33 |
3.21 |
lab |
|
|
catalytic propylene oxidation |
32 |
36 |
3.07 |
commercial |
|
|
oxalate acidification |
classic acidification |
44 |
44 |
4.29 |
commercial |
|
paired electrodialysis |
85 |
84 |
4.71 |
bench |
X=could not be calculated. [a] Atom economy=(mass of all products/mass of all reactants)×100. [b] Reaction mass efficiency=actual yield of all process steps combined×(mass of all products)/(mass of all reactants). [c] Sustainability rating is a rating on the overall sustainability of the process on a 1–5 scale, where 1 is the worst and 5 is the best achievable rating. The rating considers seven categories for which different impacts were attributed and are listed with descending impact: feedstock sustainability (Impact: 5), production of waste and greenhouse gases (Impact: 3), use of precious materials or solvents (Impact: 2), energy source process toxicity and safety concerns (Impact: 2), intensity of downstream separation (Impact: 1), energy efficiency and process conditions (Impact: 1). For all sub‐categories, a rating from 1 (worst) to 5 (best) was given. The overall rating reflects the average of the sum of grades for all categories weighted by their impact factors. [d] Maturity reflects scale at which a process is proven: lab‐scale includes non‐automized or optimized systems at low or sub gram scale (TRL 1–2); bench‐scale includes processes that are performed at a high g or kg scale with upscaling and optimization in mind (TRL 3–5); pilot‐scale includes processes that are performed at a large kg or low ton scale to demonstrate the process (TRL 5–7); commercial‐scale includes processes that have been used successfully commercially.