Method for producing synthetic gas by natural gas conversion
A technology for synthesis gas and natural gas, applied in chemical instruments and methods, inorganic chemistry, non-metallic elements, etc., can solve the problems of high operating cost, explosion of methane and oxygen mixture, and high oxidation reaction temperature
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Embodiment 1
[0025] Implementation conditions: natural gas flow rate: 100Ncm 3 / min
[0026] Air flow: 250Ncm 3 / min
[0027] Oxygen carrier dosage: 30g
[0028] Oxygen carrier particle size: 100 mesh
[0029] Fluidized bed working temperature: 850°C
[0030] Fluidized bed working pressure: 0.1MPa
[0031] Implementation results: natural gas conversion rate: 97%
[0032] Syngas H 2 Ratio to CO: 1.91
[0033] Nitrogen purity: 93%
[0034] Continuous working time of circulating fluidized bed: 125min
Embodiment 2
[0036] Implementation conditions: natural gas flow rate: 80Ncm 3 / min
[0037] Water vapor flow rate: 3.6g / min
[0038] Inlet steam temperature: 400°C
[0039] Oxygen carrier dosage: 24g
[0040] Oxygen carrier particle size: 100 mesh
[0041] Fluidized bed working temperature: 850°C
[0042] Fluidized bed working pressure: 0.1MPa
[0043] Implementation results: natural gas conversion rate: 94%
[0044] Syngas H 2 Ratio to CO: 1.97
[0045] Nitrogen purity: 93%
[0046] Continuous working time of circulating fluidized bed: 87min
Embodiment 3
[0048] Implementation conditions: natural gas flow rate: 100Ncm 3 / min
[0049] Carbon dioxide flow: 200Ncm 3 / min
[0050] Oxygen carrier dosage: 24g
[0051] Oxygen carrier particle size: 100 mesh
[0052] Fluidized bed working temperature: 800°C
[0053]Fluidized bed working pressure: 0.1MPa
[0054] Implementation results: natural gas conversion rate: 90%
[0055] Syngas H 2 Ratio to CO: 1.87
[0056] Carbon dioxide conversion rate: 76%
[0057] Continuous working time of circulating fluidized bed: 45min.
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