Ferric-carbon micro-electrolysis gas-solid-liquid three-phase reactor for purifying harmful gas
An iron-carbon micro-electrolysis and harmful gas technology, which is applied in chemical instruments and methods, air quality improvement, and separation of dispersed particles, can solve problems such as micro-electrolysis technology waste gas treatment that has not been seen, and achieve improved absorption effect and absorption capacity , the effect of simple operation
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Embodiment 1
[0015] Embodiment 1: Experimental device adopts figure 1 In the reactor structure shown, the outer body material is polypropylene, the size is 120mm×120mm×1000mm, the distance between adjacent iron grids is 50mm, the thickness of the iron grid is 2mm, and the mesh size is 5mm×5mm. The active carbon used as the mobile pole has an average geometric diameter of about 1mm, and the filling rate of the activated carbon in the liquid phase is about 10%. The simulated exhaust gas is introduced from the bottom of the reactor, and is discharged from the upper part after passing through the gas distributor and the gas-solid-liquid three-phase reaction zone.
[0016] The experimental conditions are: the absorption liquid is 2% sodium chloride aqueous solution + hydrochloric acid. Solution pH=3±0.5.
[0017] Gas flow: 2000ml / min, gas temperature: 25°C
[0018] The types of waste gas are common and representative volatile organic compounds such as hydrocarbons, alcohols, ethers, aldehyde...
Embodiment 2
[0023] Embodiment 2: Experimental device adopts figure 2 In the reactor structure shown, the reactor cylinder is made of polypropylene, with a diameter of 150 mm, an effective height of 1000 mm, and an iron Pall ring with a diameter of 25 mm and a thickness of 2 mm. The active carbon particles used as the mobile electrode have an average geometric diameter of about 1 mm, and the filling rate of the active carbon in the liquid phase is about 15%. The simulated exhaust gas is introduced from the bottom of the reactor, and is discharged from the upper part after passing through the gas distributor and the gas-solid-liquid three-phase reaction zone.
[0024] The experimental conditions are: the absorption liquid is 2% sodium sulfate aqueous solution+sulfuric acid. Solution pH=5±0.5.
[0025] Gas flow: 2000m1 / min, gas temperature: 25°C
[0026] Exhaust gas kind is the same as embodiment 1
[0027] Carrier gas: air
[0028] Experimental results: as shown in Table 2.
[0029] ...
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