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高含盐气田采出水雾化蒸发减量现场试验

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高含盐气田采出水膜处理产生了较多的浓盐水,多采用多效蒸发、机械压缩蒸发等热蒸馏法蒸发处理浓盐水,具有处理成本高、难度大等缺点。结合密闭空间蒸发和旋转雾化技术,研发出采出水蒸发中试装置。现场试验表明,在一定范围内,雾滴直径小、风速较小、雾化器高处安装有助于确保蒸发效果;同时,合适的参数选取可以避免未完全蒸发的雾滴漂移出装置。在现场试验和运行时,一种典型工况为设定3200 rpm不变频固定转速,进水流量范围1。0~1。2 m3/h,消耗电机功率1。5 kW,雾化器高度 4 m,产生的雾滴直径为150 μm。当环境温度>20℃,空气相对湿度<80%,蒸发减量率能够维持在 50%以上,可以有效实现高含盐采出水的减量处理,减小后续热蒸馏工艺负荷,降低气田采出水整体处理成本。
Field Tests of Produced Water Atomization Evaporation in a High Salinity Gas Field
The membrane treatment of produced water from high salinity gas fields produces a large amount of concentrated brine.Concentrated brine is often evaporated using thermal distillation methods such as multi effect evaporation and mechanical compression evaporation,which have the disadvantages of high processing cost and difficulty.Combined with confined space evaporation and rotary atomization technology,a pilot plant for produced water evaporation was developed.Field tests have shown that within a certain range,small droplet diameters,low wind speeds,and high installation of atomizers can help ensure evaporation efficiency.Meanwhile,appropriate parameter selection can prevent incomplete evaporation of fog droplets from drifting out of the device.During field testing and operation,a typical operating condition is to set a fixed speed of 3200 rpm without frequency conversion,with a water inlet flow range of 1.0~1.2 m3/h,a motor power consumption of 1.5 kW,a height of 4m for the atomizer,and a diameter of 150 μm droplets.When the ambient temperature is greater than 20℃and the relative humidity of the air is less than 80%,the evaporation reduction rate can be maintained at more than 50%,which can effectively achieve the reduction treatment of high salinity produced water,reduce the subsequent thermal distillation process load,and reduce the overall treatment cost of gas field produced water.

gas fieldmechanical atomizationsaline wastewaterevaporation effectfield test

唐志伟

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中国石化石油勘探开发研究院,北京 102206

气田 机械雾化 含盐废水 蒸发效果 现场试验

2024

广东化工
广东省石油化工研究院

广东化工

影响因子:0.288
ISSN:1007-1865
年,卷(期):2024.51(4)
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