Modular skid-mounted device for making oil through marsh gas
A modular and skid-mounted technology, applied in inorganic chemistry, gas fuel, petroleum industry, etc., can solve problems such as long construction period, time-consuming design, and immobile devices
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Embodiment 1
[0090] After the biogas is introduced into the inlet pipeline of the purification compression and reforming module, it first passes through a gas-liquid separator to remove the liquid droplets carried in the biogas, and then enters two series-connected desulfurization towers (built-in desulfurization agent zinc oxide), and finally passes through 2 A metal powder sintered filter with a filter element diameter of 0.2 μm connected in series can obtain biogas with sulfur content < 10 ppb, dust content < 0.5 μ m, and oil content < 10 ppm. The purified biogas enters the compression module, and under the action of a gas compressor, 0.8MPa biogas is obtained as reforming raw material gas.
[0091] The compressed biogas and compressed air enter the plasma arc reforming reactor at a volume flow ratio of 1:10. At 1050°C, Ni-Al 2 o 3 The reforming reaction takes place under the condition of catalyst and steam to convert methane into synthesis gas (H 2 / CO=2.1).
[0092] Synthesis gas (...
Embodiment 2
[0098] The process of obtaining synthesis gas is the same as in Example 1.
[0099] Synthesis gas (flow rate is 12Nm 3 / h) After entering the Fischer-Tropsch synthesis module, first pressurize it to 2.0MPa through a synthesis gas compressor. The pressurized synthesis gas enters a set of Fischer-Tropsch synthesis fixed-bed reactor with an output of 18L / day, and Fischer-Tropsch synthesis reaction occurs under the action of iron / copper / potassium / alumina catalyst (reaction temperature 265°C, space velocity 7500h -1 ), the reaction product and unreacted synthesis gas are separated by three-stage gas-liquid separation in the hot separation tank (160°C), cold separation tank (30°C) and cryogenic tank (-2°C) to obtain hydrocarbon products and gas products Most of the unreacted gas is mixed with the synthesis gas through the circulation compressor and then re-enters the reactor (the ratio of circulation gas to synthesis gas is 2.5), and a small part is discharged from the system. The...
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