Research Article
Carbon-Based Catalyst from Pyrolysis of Waste Tire for Catalytic Ethanol Dehydration to Ethylene and Diethyl Ether
Table 4
Comparison of catalysts for ethylene dehydration and their catalytic ability.
| Catalyst | Reaction temperature (°C) | Ethanol conversion (%) | Ethylene selectivity (%) | Ref. |
| HBZ | | | 200–400 | 7–100 | 1–100 | [17] | Al-HBZ | | | 200–400 | 9–92 | 0–98 | [17] | M-Al | | | 200–400 | 12–92 | 0–96 | [17] | H-ZSM-5 | | | 400 | 99 | 10 | [32] | 20HP-ZSM-5 | | | 250–450 | 25–100 | 3–98 | [32] | γ-Al2O3 | | | 400–550 | 70–100 | 40–95 | [11] | TiO2/γ-Al2O3 | | | 360–550 | 70–100 | 50–99 | [11] | SAPO-34 | | | 500 | 100 | 100 | [33] |
| Carbon based | Activator | Modifier | | | | | Bacterial cellulose | | | 200–400 | 41–65 | 0–65 | [34] | Olive stone | Steam | (NH4)2S2O8 | 180 | 1–22 | 16–26 | [35] | Polish brown coal | HCl, HF | HNO3 | 150–450 | n.a. | 0–50 | [24] | CH3COOOH | 150–450 | n.a. | 0–15 | [25] | H2SO4 | 150–450 | n.a. | 0–14 | [25] | Air | 150–450 | n.a. | 0–18 | [25] | Cl2 | 150–450 | n.a. | 0–5 | [25] | Waste tire | HCl | H2SO4 | 200–400 | 14–36 | 65–69 | This work | HNO3 | H2SO4 | 200–400 | 22–29 | 69–75 | This work |
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Based on the ethanol conversion to ethylene only and the values are approximate. |