Calculation formula for the nitrogen gas volume in theoretical stripping for NHD decarburization
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I would like to ask: the calculation formula for the amount of nitrogen to be stripped using NHD decarburization theoryParameter: Selesol, Rectisol, NHD
Electricity consumption (kWh): 60.21, 29.60, 43.41
Recycled water volume (m3): 45.59, 15.50, 12.00
Steam consumption (t): 0.85 (0.59 MPa), 0.058 (1.3 MPa), 0.306 (0.90 MPa), 0.39 (0.35 MPa)
Strip gas (N2) volume (Nm3): 684, 280, 578
Cooling energy required (GJ): 0.126 (1.5°C), 0.358 (-40°C), 0.137 (-15°C)
Solvent consumption cost (yuan): 4.0, 2.7, 4.6
Investment cost per ton of ammonia (yuan): 19.91, 17.13, 14.67
Relative investment ratio: 100, 86, 74
Operating cost per ton of ammonia (yuan): 123, 97, 115
Relative operating cost ratio: 100, 79, 93
Total cost per ton of ammonia (yuan): 142.91, 114.13, 129.67
Relative total cost ratio: 100, 80, 91