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. 2023 Jan 18;9(1):e13006. doi: 10.1016/j.heliyon.2023.e13006

Table 4.

Use of co-solvents in heterogeneous alkaline catalysed methanolysis.

Co-solvent Catalyst Reactor type Feedstock Pre-
treatment
Reaction conditions
Yield
(wt.%d)
Ref.
Co-solvent amount
(wt.%a, v.%b, mol%c)
Catalyst amount (wt.%a) MeOH/oil molar ratio Time
(min)
T
(°C)
Stirrer
(rpm)
Special
conditions
Acetone CaO
(River snail shells)
STR Palm oil 10 v.% 5 12:1 120 65 300 95.28 [72]
CaO
(scallop shells)
Flask Beef tallow/
soybean oil
(1:1)
36 v.% 150 -e 85.3 [11]
Ca2Al2O5 STR WCO 1 92 v.%
(20 wt%)
1.2 6:1 25 55 N/S 97.98f [73]
Waste cement
(calcined with
K2CO3; 1:4)
Electrolysis cell WCO 40 v.%
(10 wt%)
12 7:1 120 25 300 30 V
2 wt% water
95.5 [74]
Zeolite/chitosan/
KOH composite
Electrolysis cell WCO 40 v.%
(10 wt%)
1 180 RT 100 40 V
2 wt%
water
93 [75]
Crude
biodiesel
CaO STR Sunflower oil 34 vol%
(10 wt%)
41.5
g/Ltotal volume
7.1:1 90 52 N/S 98.9 [77]
n-hexane CaO STR Sunflower oil 110 v.%
(20 wt%)
5.82 6:1 240 60 N/S 98.8 [60]
CaO Microreactor WCO 3 58 v.% 8.17 51.3 v.%g
(1:1.95)
10 62 -e 97.03 [78]
Na/NaOH/
γ-Al2O3
STR Soybean oil 55 v.% 2.17 9:1 120 60 300 94 [79]
2-propanol CaO Packed-
microchannel
Palm oil 20 v.%
(14.5 wt%)
30 mg 20:1 6.5 65 -e 98.3 [71]
1-propanol CaO
(River snail shells)
STR Palm oil 10 v.% 5 12:1 120 65 300 95.69 [72]
90 94.44
THF CaO
(waste crab shells)
STR Fish oil 3 100 v.% 2.5 10:1 90 65 650 95 [80]
CaO
(River snail shells)
STR Palm oil 10 v.% 5 12:1 120 65 300 96.68 [72]
CaO STR Rapeseed oil 62 v.%
(30 wt%)
2.5 12:1 360 60 600 97 [81]
ZnO–Sr(NO3)2 STR Soybean oil 91 v.%
(44.5 wt%)
5 12:1 240 65 N/S 96.8f [82]
CaO STR Sunflower oil 82 v.%
(20 wt%)
5.82 6:1 240 60 N/S 98.1 [60]
Limescale Microreactor WCO 3 62 v.% 8.13 50.8 v.%g
(1:1.97)
10 64.5 -e 95.21 [78]
Zeolite/chitosan/
KOH composite
Electrolysis cell WCO 35 v.%
(10 wt%)
1 7:1 180 RT 100 40 V
2 wt%
water
93 [75]

1: filtrated and dried.

2: filtration, drying and esterification.

3: esterification.

a

regarding the oil weight.

b

regarding the MeOH volume.

c

regarding mole MeOH.

d

%FAME yield.

e

no agitation.

f

% oil conversion.

g

regarding the oil volume.