Skip to main content
. 2022 Dec 2;123(9):6359–6411. doi: 10.1021/acs.chemrev.2c00439

Table 2. Conditions and Performances of the Two-Step Stoichiometric Methane-to-Methanol Reaction on Various Cu Modified Zeolites.

          O2 CH4 CH4 methanol methanol    
entry zeolite Si/Al ratio Cu/Al ratio preparation activation T (°C) reaction T (°C) pressure (bar) productivity (μmol g–1) selectivity (%) extraction method ref
1 ZSM-5 12 0.1 IE 450 175 1 0   a (335)
2 ZSM-5 12 0.22 IE 450 175 1 1.27   a (335)
3 ZSM-5 12 0.25 IE 450 175 1 3.8   a (335)
4 ZSM-5 12 0.32 IE 450 175 1 8.9   a (335)
5 ZSM-5 12 0.42 IE 450 175 1 9   a (335)
6 ZSM-5 12 0.54 IE 450 175 1 8.2   a (335)
7 ZSM-5 12 0.58 IE 450 175 1 8.2 98 a (335)
8 ZSM-5 12 0.54 IE 450 150 1 8.19   a (336)
9 ZSM-5 25 0.51 IE 450 150 1 4.1   a (336)
10 ZSM-5 30 0.47 IE 450 150 1 2.7   a (336)
11 ZSM-5 77.5 0.55 IE 450 150 1 0.9   a (336)
12 ZSM-5 120 0.88 IE 450 150 1 0.66   a (336)
13 ZSM-5 11.5 0.34 IE 450 200 1 16   b (337)
14 ZSM-5 11.6 0.53 IE 400 200 8 31 52 a (338)
15 ZSM-5 11.6 0.53 IE 400 360 8 0   a (338)
16 Na-ZSM-5 14 0.65 IE 450 200 1 9   a (339)
17 MOR 5.3 0.39 IE 450 150 1 3.6   a (336)
18 MOR 5.3 0.39 IE 450 200 1 13   a (336)
19 MOR 8.8 0.5 IE 450 150 1 6   a (336)
20 MOR 8.8 0.43 IE 450 175 1 11.34   a (335)
21 MOR 8.8 0.5 IE 450 200 1 16   a (336)
22 MOR 5 0.34 IE 450 200 1 31   b (337)
23 MOR 10.5 0.39 IE 400 200 8 119 91 a (338)
24 MOR 10.5 0.39 IE 400 360 8 5   a (338)
25 MOR 10 0.27 SSIE 450 200 1 37.3   a (340)
26 MOR 10 0.27 SSIE 550 200 1 55.3   a (340)
27 MOR 10 0.27 SSIE 650 200 1 65.2   a (340)
28 Na-MOR 5 0.3 IE 450 200 1 21   a (339)
29 Na-MOR 8.5 0.38 IE 450 200 1 25.8   a (339)
30 Y 2.7 0.05 IE 450 175 1 <1   a (335)
31 Y 2.7 0.29 IE 450 175 1 <1   a (335)
32 Y 2.7 0.45 IE 450 200 1 <1   a (336)
33 Na-Y 3 0.32 IE 450 200 1 <1   a (339)
34 Y 2.6 0.41 IE 400 360 1 90 91 a (338)
35 Y 2.6 0.41 IE 400 360 1 88 92 b (338)
36 Y 2.6 0.41 IE 400 360 8 303 93 b (338)
37 Y 2.6 0.41 IE 400 360 15 360 93 b (338)
38 USY 27.5 0.32 IE 450 200 1 <1   a (336)
39 EMT 4 0.36 IE 450 150 1 <1   a (336)
40 FER 6.2 0.42 IE 450 150 1 1.6   a (336)
41 FER 6.2 0.42 IE 450 200 1 12   a (336)
42 Na-FER 8.9 0.38 IE 450 200 1 10.4   a (339)
43 BEA 9.8 0.5 IE 450 150 1 1.6   a (336)
44 BEA 9.8 0.5 IE 450 200 1 4.2   a (336)
45 BEA 12.4 0.4 IE 400 200 8 55 98 a (338)
46 BEA 12.4 0.4 IE 400 360 8 8   a (338)
47 SSZ-13 6 0.35 IE 450 200 1 28   b (337)
48 SSZ-13 12 0.35 IE 450 200 1 31   b (337)
49 Na-SSZ-13 15.8 0.84 IE 450 200 1 30   a (339)
50 SSZ-16 6.5 0.34 IE 450 200 1 39   b (337)
51 SSZ-36 10 0.26 IE 450 200 1 36   b (337)
52 SAPO-34 6 0.6 IE 450 200 1 15   b (337)
53 OME 3.2 0.07 IE 450 200 1 1.9   a (339)
54 Na-OME 3.2 0.12 IE 450 200 1 17.7   a (339)
55 Na-OME 3.2 0.29 IE 450 200 1 86.1   a (339)
56 Na-OME-fast 4.3 4.78 wt % IE 450 200 1 ca. 100   a (341)
57 Na-OME-slow 4.3 4.64 wt % IE 450 200 1 150.9   a (341)
58 ECR 3.5 0.09 IE 450 200 1 2.6   a (340)
59 Na-ECR 3.5 0.14 IE 450 200 1 9   a (340)
60 Na-ECR 3.5 0.33 IE 450 200 1 19.7   a (340)
a

Extraction of methanol with water at ambient temperature.

b

Desorption of methanol in a stream of wet inert gases at an elevated temperatures ≥200 °C.