Treatment process of mercury-containing production waste water from exploitation of natural gas field
A technology for waste water production and treatment process, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. Simple and stable process, good removal effect
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Embodiment 1
[0033] A treatment process for mercury-containing production waste water from natural gas field development, comprising the following steps:
[0034] (1) Pretreatment: The production wastewater with a chloride ion concentration of less than 30,000mg / L, a total mercury concentration of less than 20mg / L, and a chemical oxygen demand of less than 10,000mg / L is pretreated by degreasing and dewaxing to oil below 100mg / L, and the pH is adjusted The value is 3-6;
[0035] (2) Micro-electrolysis treatment: The pretreated production wastewater is treated by iron-carbon micro-electrolysis. The micro-electrolysis treatment focuses on removing toxic and harmful substances such as inorganic mercury and alkyl mercury in natural gas field wastewater, and at the same time degrades difficult degrade organic matter;
[0036] (3) Catalytic oxidation treatment: Add hydrogen peroxide, such as industrial hydrogen peroxide, to the water after the iron-carbon micro-electrolysis treatment in step (2)...
Embodiment 2
[0042] 60L of natural gas field development and production wastewater containing 28000mg / l of chloride ions, 19mg / L of total mercury, 57ng / L of alkylmercury, and 9300mg / L of chemical oxygen demand from which oil and paraffin have been removed, adjusted the pH with sulfuric acid The value is 3.1, and the metering pump is continuously used to enter the iron-carbon micro-electrolysis tower equipped with iron-carbon micro-electrolysis filler at a speed of 2L / h, and the effluent naturally flows into the catalytic oxidation kettle; 6g of metal catalyst (containing 3% active ingredient) is added to the catalytic oxidation kettle and 1200mL of industrial hydrogen peroxide with a mass concentration of 27.5%, adjust the pH value to 3.2 with 20% sulfuric acid, react intermittently for 12 hours, and then flow into the flocculation reaction tank, add a coagulant solution containing 180g of ferric chloride, and then add lime emulsion Adjust the pH value to 9.6, add 60mL of 0.1% cationic poly...
Embodiment 3
[0044] Natural gas fields where oil has been removed (oil content less than 10mg / l), paraffin containing chloride ions is 16000mg / l, total mercury is 14.5mg / L, alkylmercury is 57ng / L, and chemical oxygen demand is 6900mg / L Develop 60L of mercury-containing production wastewater to adjust the pH value to 4.0 with sulfuric acid, and continuously use a metering pump to enter the iron-carbon micro-electrolysis tower equipped with iron-carbon micro-electrolysis fillers at a speed of 3L / h, and the effluent naturally flows into the catalytic oxidation kettle; 3g of metal catalyst (containing 2% active ingredient) and 450mL of industrial hydrogen peroxide with a mass concentration of 27.5%, adjust the pH value to 4.0 with 20% sulfuric acid, stir intermittently for 8 hours and then flow into the flocculation reaction tank, add 600g of ferrous sulfate Coagulant solution, then add lime emulsion to adjust the pH value to 8.7, add 50mL of cationic polyacrylamide solution with a mass concent...
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