A method for increasing the viscosity of polymer solution prepared from oilfield sewage
A technology for preparing polymers and oilfield sewage, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc. It is difficult to maintain and use, and the composition of oilfield sewage is complex, so as to achieve the effect of easy control and maintenance, low treatment and operation cost, and low cost
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Embodiment 1
[0020] Taking biochemical sewage from an oil field, the sewage is first filtered through a multi-media filter to remove some suspended solids, etc., and then enters the ultrafiltration system. The ultrafiltration membrane material is polyvinylidene fluoride (PVDF), and the filtration method is full-flow filtration. The flux is 50 L / m 2 ·H, the water after ultrafiltration and filtration enters the ion exchange equipment, the resin used is the bleach softening cation resin (001*7), the working speed is 20m / h, and then it is filled with nitrogen and deoxygenated to dissolve in the sewage The oxygen content is less than 0.5 mg / L, and the water quality comparison results before and after oilfield sewage treatment are shown in Table 1. The polymer PAM1 was prepared with oilfield sewage before and after treatment, and the polymer concentration was 1500 mg / L. The initial viscosity of the solution and the stability of the solution viscosity at 80°C were measured. The measurement time was...
Embodiment 2
[0026] In addition, the biochemical wastewater from an oil field is directly filtered in the ultrafiltration system. The ultrafiltration adopts cross-flow filtration. The recovery rate of the system is 92% and the operating flux is 60 L / m. 2 ·H, the sewage filtered by ultrafiltration enters the ion exchange equipment, the resin used is DOWEX? MARATHON? C, the working speed is 17m / h, after the resin is treated, the sewage is deoxygenated with a deaerator to make the sewage dissolved The oxygen content is less than 0.5 mg / L, and the water quality comparison results before and after oilfield sewage treatment are shown in Table 3. The polymer PAM2 was prepared with oilfield sewage before and after treatment, and the polymer concentration was 1000 mg / L. The initial viscosity of the solution and the stability of the solution viscosity at 80℃ were measured. The measurement time was 10 days. The comparison results are shown in Table 4.
[0027] table 3
[0028] Analysis Project
[0029...
PUM
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