Freon treated by premixed combustion and method for producing said resource
A pre-mixed combustion and freon technology, applied in the direction of combustion method, combustion type, incinerator, etc., can solve the problems of unstable freon decomposition rate, low carbon dioxide selectivity, incomplete freon decomposition, etc., to improve flame propagation speed and combustion Effects of increasing temperature and decomposition rate and reducing fuel consumption
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Embodiment 1
[0040] Commercially available Freon-12 (F-12, namely difluorodichloromethane CCl 2 f 2 ). For Freon-12, m, n, and p in formula (a) are 1, 0, and 4 respectively, then formula (a) becomes:
[0041] CCl 2 f2 +2H 2 O→CO 2 +2HF+2HCl (c)
[0042] Use civil liquefied petroleum gas as fuel.
[0043] The incinerator cavity is a cylindrical cavity with a diameter of 120mm and a length of 1000mm.
[0044] The flow velocity of the premixed gas in the heat exchange tube is 5.6M / s, and the flow velocity of the combustion exhaust gas in the premixer is 1.5M / s.
[0045] First of all, according to the design processing capacity range of the incinerator, the processing capacity of Freon is determined to be 0.01M 3 / min; According to formula (1), it is determined that Freon: the molar ratio of fuel = 1: 1, that is, the liquefied petroleum gas flow rate is 0.01M 3 / min; determined according to formula (2) That is, the water vapor flow rate is 0.005M 3 / min; 1M 3 The theoretical air v...
Embodiment 2
[0051] Commercially available Freon-13 (F-13, that is, trifluorochloromethane CClF 3 ). For Freon-13, m, n, and p in formula (a) are 1, 0, and 4 respectively, and formula (a) is:
[0052] CCIF 3 +2H 2 O→CO 2 +3HF+HCl (d)
[0053] Use artificial gas (the main component is carbon monoxide) as fuel.
[0054] Incinerator is the same as embodiment 1.
[0055] First of all, according to the design processing capacity range of the incinerator, the processing capacity of Freon is determined to be 0.012M 3 / min, according to formula (1) to determine Freon: fuel molar ratio = 1: 7.5, that is, the artificial gas flow rate is 0.09M 3 / min, determined according to formula (2) That is, the water vapor flow rate is 0.036M 3 / min, 1M 3 The theoretical air volume required for artificial gas combustion is 18.51M 3 , taking the excess air coefficient of liquefied petroleum gas combustion as 1.1, and the primary air volume accounts for 70% of the total air volume, the total air volume...
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