Electrochemistry method for treating oilfield produced water into confecting polymer water
A technology for producing water, mixing and gathering water, applied in chemical instruments and methods, water/sewage treatment, water/sewage multi-stage treatment, etc., to achieve wide adaptability, easy promotion and application, and easy operation
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Embodiment 1
[0034] In this embodiment, the electrochemical method is used to feed unidirectional continuous direct current to the oilfield sewage to treat the oilfield produced water of a certain sewage station, and the treatment flow rate is 238m 3 / h. The voltage between each pair of negative and positive electrodes is 5.12V, and the current is 3840A. The 4 pairs of electrodes are connected in parallel, and the total electrode area is 1.28m 2 , the current density is 3000A / m 2 The distance between each pair of negative and positive electrode plates is 50 mm, and the space between each pair of negative and positive electrodes is filled with polystyrene resin containing carboxylate. The anode material is a composite electrode of titanium, ruthenium, rhodium, and iridium, and the cathode material is For stainless steel. The anode will reduce the reducing substances in the oilfield produced water, such as Fe 2+ , S 2- Plasma and FeS colloids are oxidized and hydrolyzed into colloidal Fe...
Embodiment 2
[0039] In this embodiment, the electrochemical method is used to feed regular reverse continuous direct current to the oilfield sewage to treat the oilfield produced water of a certain sewage station, and the treatment flow rate is 354m 3 / h. The voltage between each pair of cathode and anode electrodes is 4.37V, the current is 6724A, 21 pairs of electrodes are connected in parallel, and the total electrode area is 6.72m 2 , the current density is 1000A / m 2 , the distance between each pair of negative and positive electrode plates is 20 mm, and the space between each pair of negative and positive electrodes is filled with polystyrene resin containing sulfonate. The anode material is iron, aluminum, platinum, and the cathode material is stainless steel. The anode will reduce the reducing substances in the oilfield produced water, such as Fe 2+ , S 2- Plasma and FeS colloids are oxidized and hydrolyzed into colloidal Fe x (OH) m (3x-m)+ and elemental sulfur, while complete...
Embodiment 3
[0044] In this embodiment, the electrochemical method is used to feed unidirectional pulse direct current to the oilfield sewage to treat the oilfield produced water in a certain sewage station, and the treatment flow rate is 430m 3 / h. The voltage between each pair of cathode and anode is 1V, and the current is 5497A. In this embodiment, there are 26 pairs of electrodes, the first group has 13 pairs of electrodes connected in parallel, the second group has 13 pairs of electrodes connected in parallel, and then the two groups are connected in series; the total area of the electrodes is 8.32m 2 , the current density is 1602A / m 2 The distance between each pair of negative and positive electrode plates is 25 mm, and the space between each pair of negative and positive electrodes is filled with polystyrene resin containing quaternary ammonium salts. The anode material is a composite electrode of titanium, ruthenium, platinum, and ruthenium, and the cathode material is For stai...
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