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Evaluation of In-Situ Generated Acids for Filter-Cake Cleanup

机译:评估原位产生的酸以净化滤饼

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Filter cake removal is a difficult task, especially in horizontal and extended reach wells. Water-based drilling fluids consist of xanthan gum as a viscosifier, starch as a fluid-loss control, sized calcium carbonate or salt particles to increase the mud density. Conventional chemical means used to remove filter cake are reactive mineral acids, enzymes, chelating agents, oxidizers, or combinations of these chemicals. Controlling of the reaction rate of the cleaning fluids with the filter cake material is an essential factor that determines the efficiency of filter cake removal. This study assesses the performance of three acid precursors (esters) that produce organic acids. These precursors produce low-molecular weight organic acids that can dissolve calcium carbonate particles from the filter cake. The rate of hydrolysis of acid precursors can be adjusted to produce a predetermine acid concentration at bottom hole conditions. Enzymes, mainly α-amylase, can be added to these esters to break starch that is present in the filter cake. The slow release of these weak organic acids ensures proper and efficient removal of the filter cake. Lab studies using static HPHT filter press indicated that the three systems can remove the filter cake efficiently. The rate of hydrolysis was measured for each system, and found to be a function of temperature and type and concentration of the acid precursor. Surface tension measurements conducted for solutions of the three precursors at different temperatures highlighted low surface tension values for the spent acids, which are needed to lift the spent acid following the treatment. No phase separation or precipitation was observed when the three systems were heated at temperatures up to 250°F. Surface tension measurements indicated that the formic acid system had low surface tension, which will accelerate lifting these fluids from tight formations. Acetic and lactic acid systems had much higher surface tension, and a suitable surfactant will be needed to reduce the surface tension. The kinetic study indicated the very rapid reaction rate of the precursor of formic acid and a moderate reaction rate in the acetic acid system. The reaction rate of the precursor of lactic acid was in between the two systems and more close to the in-situ acetic acid system. HPHT experiments showed that formic acid system was very efficient at short soaking times at temperatures of 200 and 250°F. The performance of lactic acid was comparable to formic acid when the soaking time was increased from 4 to 6.75 hrs. The efficiency of acetic acid was much lower than the other two acids. Acetic acid will require much longer soaking times.
机译:滤饼的去除是一项艰巨的任务,尤其是在水平井和扩展井中。水性钻井液由黄原胶(作为增粘剂),淀粉(作为防漏失剂),大小合适的碳酸钙或盐颗粒组成,以增加泥浆密度。用于去除滤饼的常规化学方法是反应性无机酸,酶,螯合剂,氧化剂或这些化学物质的组合。控制清洗液与滤饼材料的反应速率是决定滤饼去除效率的重要因素。这项研究评估了产生有机酸的三种酸前体(酯)的性能。这些前体产生低分子量有机酸,可以溶解滤饼中的碳酸钙颗粒。可以调节酸前体的水解速率,以在井底条件下产生预定的酸浓度。可以将酶(主要是α-淀粉酶)添加到这些酯中,以破坏存在于滤饼中的淀粉。这些弱有机酸的缓慢释放可确保正确,有效地除去滤饼。使用静态HPHT压滤机的实验室研究表明,这三个系统可以有效地去除滤饼。测量每个系统的水解速率,发现水解速率是温度,酸前体的类型和浓度的函数。对三种前体在不同温度下的溶液进行的表面张力测量突出显示了废酸的低表面张力值,这对于处理后提升废酸是必需的。当三个系统在最高250°F的温度下加热时,未观察到相分离或沉淀。表面张力测量表明,甲酸体系​​的表面张力较低,这将加速将这些流体从致密地层中提起。乙酸和乳酸体系的表面张力要高得多,因此需要合适的表面活性剂来降低表面张力。动力学研究表明,甲酸前体的反应速度非常快,在乙酸体系中反应速度中等。乳酸前体的反应速率介于两种体系之间,更接近于原位乙酸体系。 HPHT实验表明,在200和250°F的温度下,甲酸体系​​在短时间浸泡中非常有效。当浸泡时间从4小时增加到6.75小时时,乳酸的性能可与甲酸媲美。乙酸的效率远低于其他两种酸。乙酸将需要更长的浸泡时间。

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