宋金仕, 欧绍祥, 单正名, 张国强. 循环泡沫钻井工艺技术的应用[J]. 石油钻采工艺, 1998, 20(6): 24-28. DOI: 10.3969/j.issn.1000-7393.1998.06.009
引用本文: 宋金仕, 欧绍祥, 单正名, 张国强. 循环泡沫钻井工艺技术的应用[J]. 石油钻采工艺, 1998, 20(6): 24-28. DOI: 10.3969/j.issn.1000-7393.1998.06.009
Song Jinshi, Ou Shaoxiang, Shan zhengming, Zhang Guoqiang. APPLICATION OF CIRCULATION FOAM DRILLING TECHNOLOGY[J]. Oil Drilling & Production Technology, 1998, 20(6): 24-28. DOI: 10.3969/j.issn.1000-7393.1998.06.009
Citation: Song Jinshi, Ou Shaoxiang, Shan zhengming, Zhang Guoqiang. APPLICATION OF CIRCULATION FOAM DRILLING TECHNOLOGY[J]. Oil Drilling & Production Technology, 1998, 20(6): 24-28. DOI: 10.3969/j.issn.1000-7393.1998.06.009

循环泡沫钻井工艺技术的应用

APPLICATION OF CIRCULATION FOAM DRILLING TECHNOLOGY

  • 摘要: 常规泡沫低压钻井工艺技术存在两个问题,一是泡沫的一次性使用.使泡沫钻井成本大大增加、同时严重污染环境;二是由于泡沫流体的可压缩性,随着地面温度、压力的变化,井下泡沫质量、密度等参数也随之变化,增加了施工参数设计计算的复杂性。为解决以上两个问题,优选了泡沫液配方,采用了循环泡沫系统装备流程,使泡沫基液可循环使用,而空气排放到大气中。根据泡沫钻井中井口注入压力、最小泡沫液流量和气体流量、泡沫液柱压力等设计参数,考虑了影响泡沫钻井作业中包含的5个方面的因素:1.将泡沫中的气体组分视为非理想气体,用Hall-Yaro-brough方法计算气体的偏差系数Z;2.由于固相碰撞和摩擦所造成的摩擦损失;3.岩屑的临界下沉速度;4.规定了井口最大泡沫质量为0.96,井底最小泡沫质量为0.55;5.根据岩屑的下沉速度确定气液排量,并规定在同一井深,泡沫流动速度应高出岩屑下沉速度10%,作为安全附加系数。对施工参数进行了系统的计算,并编制了软件程序。经现场6井次施工,均获得成功。

     

    Abstract: There were two problems exist in conventional foam low-pressure drilling technology. One problem was that the foam can only be used once, this made the foam drilling cost increase greatly, moreover, pollute the environment seriously;Another problem was that parameters like quallty, density of downhole foam and so on changed with the change of surface temperature and pressure because of the compressibility of foam. This made the job design complicated. In order to solve the two problems, the formulation of foam was optimized. The adoption of circularing foam system equipment made foam be used many times but air can be emitted into atmosphere. According to the wellhead injection pressure, minimum flow rate of foam and gas, foam column pressure and so on, 5 factors influenced foam drilling operation were taken into account:1. Taking the gas component of foam as non-ideal gas, the deviation factor Z of gas can be calculated by using Hall-Yarobrough method;2. The friction loss resulted from solid collision and friction;3. Critical submerged speed of detritus;4. The wellhead maximum foam quality was set at 0. 96, the downhole minimum foam quallty was 0. 55;5. Gas/llquid flow rate was determined by submerged speed of detritus. And stipulated that the flowing velocity of foam should be 10% higher than submerged speed at the same depth. 10% was regarded as safety additional factor. Job parameters were calculated systematically and computer software were designed. Six wells were executed on site with all of them succeeded.

     

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