Open Access

Table A.1

Overview of the main studies published over the 50 past year on the pyrolysis of methanol.

Reference Reactor Temperature range (K) Pressure Equivalence ratio
Cooke et al. (1971) A 1570–1879 1 atm 1.00
Bowman (1975) A 1545–2180 0.18–0.46 MPa 0.375–6.0
Akrich et al. (1978) F 298 0.11 atm 0.77–1.53
Aronowitz et al. (1979) B 1070–1225 0.1 MPa 0.03–3.16
Westbrook & Dryer (1979) A-B 1000–2180 0.1–0.5 MPa 0.05–3.0
Tsuboi & Hashimoto (1981) A 1200–1800 0.2–2.0
Natarajan & Bhaskaran (1981) A 1300–1700 0.25–0.45 MPa 0.5–1.5
Cathonnet et al. (1982) D 700–900 0.02–0.05 MPa 0.5–4.0
Metghalchi & Keck (1982) F 300–500 0.1 MPa 0.5–1.4
Yano & Ito (1983) C 700–1000
Cribb et al. (1984) A 2000 0.04 MPa
Hidaka et al. (1989) A 1372–1842
Norton & Dryer (1989) B 1025–1090 0.1 MPa 0.6–1.6
Chen (1991) D
Egolfopoulos et al. (1992) A-B-E-F 820–2180 0.005–0.47 MPa 0.05
Grotheer et al. (1992) C-F
Held & Dryer (1994) B 810–1043 1–10 atm 0.60–1.60
Aniolek & Wilk (1995) D 650–700 0.92 atm 0.50–1.50
Fieweger et al. (1997) A 800–1200 12.83–39.48 atm 1.00
Held & Dryer (1998) A-B-E-F 633–2050 0.026–2 MPa 0.05–2.6
Alzueta et al. (2001) B 700–1500 1 atm 0.07–2.70
Lindstedt & Meyer (2002) A-B-F
Ing et al. (2003) B 873–1073 1–5 atm 0.75–1.00
Ing et al. (2003) B 1073 1–10 atm
Rasmussen et al. (2008) B 650–1350 1.00 atm 0.004–0.08
Liao et al. (2006) D 300-550 0.1 MPa 0.6–1.4
Dayma et al. (2007) D 700–1090 10 atm 0.30–1.00
Li et al. (2007) A-B-F 300–2200 0.1–2 MPa 0.05–6.0
Noorani et al. (2010) A 1068–1776 2–12 atm 0.50–2.00
Veloo et al. (2010) C 343 1 atm 0.70–1.50
Kumar & Sung (2011) C 850–1100 6.91–29.61 atm 0.25–1.00
Aranda et al. (2013) B 600–900 20–100 atm 4.35–0.06
Ren et al. (2013) A 1200–1650 0.1–0.3 MPa
Burke et al. (2016) A-C 820–1650 0.2–5 MPa 0.5–2.0

Notes. Reactor types are as follows: shock tube (A), plug flow reactor (B), rapid compression machine (C), stirred reactor (D), static reactor (E), premixed flame (F).

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