Novel Landfill-Gas-to-Biomethane Route Using a Gas-Liquid Membrane Contactor for Decarbonation/Desulfurization and Selexol Absorption for Siloxane Removal

被引:0
|
作者
da Cunha, Guilherme Pereira [1 ]
de Medeiros, Jose Luiz [1 ]
de Queiroz F Araujo, Ofelia [1 ]
机构
[1] Univ Fed Rio de Janeiro, Escola Quim, BR-21941909 Rio De Janeiro, RJ, Brazil
关键词
landfill-gas; biomethane; CO2; removal; H2S removal; gas-liquid membrane contactor; siloxane removal; CARBON-DIOXIDE CAPTURE; RICH NATURAL-GAS; CO2; CAPTURE; PERFORMANCE EVALUATION; BIOGAS PURIFICATION; AQUEOUS-SOLUTIONS; H2S ABSORPTION; MASS-TRANSFER; SHALE GAS; WATER;
D O I
10.3390/pr12081667
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A new landfill-gas-to-biomethane process prescribing decarbonation/desulfurization via gas-liquid membrane contactors and siloxane absorption using Selexol are presented in this study. Firstly, an extension for an HYSYS simulator was developed as a steady-state gas-liquid contactor model featuring: (a) a hollow-fiber membrane contactor for countercurrent/parallel contacts; (b) liquid/vapor mass/energy/momentum balances; (c) CO2/H2S/CH4/water fugacity-driven bidirectional transmembrane transfers; (d) temperature changes from transmembrane heat/mass transfers, phase change, and compressibility effects; and (e) external heat transfer. Secondly, contactor batteries using a countercurrent contact and parallel contact were simulated for selective landfill-gas decarbonation/desulfurization with water. Several separation methods were applied in the new process: (a) a water solvent gas-liquid contactor battery for adiabatic landfill-gas decarbonation/desulfurization; (b) water regeneration via high-pressure strippers, reducing the compression power for CO2 exportation; and (c) siloxane absorption with Selexol. The results show that the usual isothermal/isobaric contactor simplification is unrealistic at industrial scales. The process converts water-saturated landfill-gas (CH4 = 55.7%mol, CO2 = 40%mol, H2S = 150 ppm-mol, and Siloxanes = 2.14 ppm-mol) to biomethane with specifications of CH4MIN = 85%mol, CO2MAX = 3%mol, H2SMAX = 10 mg/Nm(3), and Siloxanes(MAX) = 0.03 mg/Nm(3). This work demonstrates that the new model can be validated with bench-scale literature data and used in industrial-scale batteries with the same hydrodynamics. Once calibrated, the model becomes economically valuable since it can: (i) predict industrial contactor battery performance under scale-up/scale-down conditions; (ii) detect process faults, membrane leakages, and wetting; and (iii) be used for process troubleshooting.
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页数:35
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