Method for removing hydrogen sulfide from gas
A technology for removing gas and hydrogen sulfide, applied in combustible gas purification, chemical instruments and methods, combustible gas purification/transformation, etc., can solve problems such as sulfur plugging, large floor area, and large equipment investment, and achieve sulfur plugging towers The effect of reduced pressure, reduced absorption pressure, and large operating flexibility
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Embodiment 1
[0024] Example 1: The hydrogen sulfide in the gas is removed by using the complex iron solvent of the present invention, the gas enters the washing pipe from top to bottom, the desulfurization liquid passes through the nozzle, and is sprayed in reverse direction from bottom to top to the gas, gas-liquid two-phase The medium collides at high speed in the washing pipe, and when the momentum of the gas-liquid two-phase medium reaches equilibrium, a highly turbulent foam zone is formed, in which the gas-liquid two-phase not only has a large contact area, but also the contact surface is quickly renewed, thus Enhanced heat transfer and mass transfer efficiency to achieve efficient washing effect. The use of large-diameter nozzles is not prone to sulfur clogging. This process uses the washing technology in the foam area, and does not need to atomize the washing liquid. The nozzle is mainly to ensure that the washing liquid has sufficient flow on the washing pipe plane and is evenly d...
Embodiment 2
[0035] Embodiment 2: test method is the same as embodiment 1
[0036] (1) Test conditions
[0037] Prepare the concentration of hydrogen sulfide with water gas to 15.7 g / ·Nm 3 the test gas.
[0038] Test gas flow rate: 1 Nm 3 / Hour
[0039] Gas pressure: 10kpa
[0040] Nozzle flow: 12 liters / hour
[0041] Packed tower flow: 7 liters / hour
[0042] Absorption and regeneration temperature: ~40 o C
[0043] Solution pH 8.2
[0044] (2) Desulfurization effect
[0045] Under the above test conditions, continuous ventilation for 24 hours, the average content of hydrogen sulfide in the outlet gas of the dynamic wave absorber measured during the absorption process is 1500mg· / Nm 3 . The average content of hydrogen sulfide in the outlet gas of the packed tower is 14mg / Nm 3
Embodiment 3
[0046] Embodiment 3: test method is the same as embodiment 1
[0047] (1) Test conditions
[0048] Prepare the concentration of hydrogen sulfide with carbon dioxide-containing gas to 25.8 g / ·Nm 3 the test gas.
[0049] Test gas flow rate: 1 Nm 3 / Hour
[0050] Gas pressure: 10kpa
[0051] Nozzle flow: 18 liters / hour
[0052] Packed tower flow: 12 liters / hour
[0053] Absorption and regeneration temperature: ~40 o C
[0054] Solution pH 8.2
[0055] (2) Desulfurization effect
[0056] Under the above test conditions, continuous ventilation for 24 hours, the average content of hydrogen sulfide in the outlet gas of the dynamic wave absorber during the absorption process is 2200mg· / Nm 3 . The average content of hydrogen sulfide in the outlet gas of the packed tower is 19mg / Nm 3
[0057] The invention provides a relatively suitable method and device for sulfur recovery of low-pressure coal gas, associated gas and acid gas.
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