Treatment and resource technology for organic waste water
A technology for organic wastewater treatment and organic wastewater, applied in water/sewage treatment, water/sludge/sewage treatment, physical/chemical process catalyst, etc., can solve the problems of post-treatment, low hydrogen production efficiency and insignificant effect, etc. Achieve the effect of low wastewater treatment cost, high resource utilization efficiency and simple process
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Embodiment 1
[0037] Add 5 grams of Raney nickel catalysts in the fixed-bed reactor, and the phenol solution containing 0.001mol / L flows through the reactor with a flow rate of 0.1mL / min (the liquid hourly space velocity is 1.41 hours -1 ), the adjustment reaction temperature is 270 ℃, reaction pressure 5.5MPa, the liquid collected at the reactor outlet is quantitatively analyzed with Shimadzu gas chromatography (FID, area normalization method), and the transformation rate of phenol is 100%; Gas chromatography (TCD, external standard method) detects that the productive rates of hydrogen and methane in the gas phase are respectively: 0.29 and 0.2 μmol / min, the content of carbon dioxide and carbon monoxide is below the chromatographic detection limit, and the selectivity of hydrogen is 27%.
Embodiment 2
[0039] Add 5 grams of Raney nickel catalysts in the fixed-bed reactor, and the phenol solution containing 0.001mol / L flows through the reactor with a flow rate of 0.05mL / min (the liquid hourly space velocity is 0.7 hours -1 ), the adjustment reaction temperature is 270 ℃, reaction pressure 5.5MPa, the liquid collected at the reactor outlet is quantitatively analyzed with Shimadzu gas chromatography (FID, area normalization method), and the transformation rate of phenol is 100%; Gas chromatography (TCD, external standard method) detects that the productive rates of hydrogen and methane in the gas phase are respectively: 0.14 and 0.1 μmol / min, the content of carbon dioxide and carbon monoxide is below the chromatographic detection limit, and the selectivity of hydrogen is 25%.
Embodiment 3
[0041] Add 5 grams of Raney nickel catalysts in the fixed-bed reactor, and the phenol solution containing 0.001mol / L flows through the reactor with a flow rate of 0.1mL / min (the liquid hourly space velocity is 1.41 hours -1 ), the adjustment reaction temperature is 260 ℃, and the reaction pressure is 4.7MPa, and the liquid collected at the reactor outlet is quantitatively analyzed by Shimadzu gas chromatography (FID, area normalization method), and the transformation rate of phenol is 100%; Gas chromatography (TCD, external standard method) detects that the productive rates of hydrogen and methane in the gas phase are respectively: 0.48 and 0.16 μmol / min, the content of carbon dioxide and carbon monoxide is below the chromatographic detection limit, and the selectivity of hydrogen is 43%.
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