“…Dagaut et al [27] studied the oxidation of PODE 1 on a jet stirred reactor at a pressure of 5.07 bar, temperature of 800-1200 K, and equivalence ratios (φ) of 0.444, 0.889, and 1.778, respectively, and obtained the concentration distribution of some intermediate components; Sun and Wang et al [28] studied the component concentration variation of the combustion process of PODE 3 /O 2 at low pressure (p = 33.3 mbar) and 50% argon dilution in a McKenna burner; Sun and Tao et al [29] studied the reaction pathways and the concentration distribution of intermediate components in PODE 1 /O 2 /Ar mixtures at low pressure, lean combustion (p = 750 Torr; φ = 0.5), and high-pressure conditions (p = 10 atm, φ = 0.2, 0.5, and 1.5) on a jet stirred reactor; Vermeire et al [30] studied the oxidation of PODE 1 on a jet stirred reactor at a pressure of 1.07 bar, temperature of 500-1000 K, and φ of 0.25, 1.0, 2.0, and ∞, respectively; Golka et al [31] studied the single-molecule pyrolysis of PODE 1 at a pressure of 1 bar and a temperature of 1000-1700 K. The concentrationtime profiles of important intermediate components such as CO, CH 2 O, and C 2 H 6 were recorded; Peukert et al [32] measured the product distribution during the decomposition of PODE 1 at a pressure of 1.2-2.5 bar and a temperature of 1100-1430 K in a shock tube. Gaiser et al [33] investigated the effect of different CH 2 O polymerization levels on the component concentration distribution during laminar flame of PODE at low pressures in a McKenna burner.…”