无伤害压裂液的研究与应用_英文_

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清洁聚合物压裂液研究与现场应用

清洁聚合物压裂液研究与现场应用

清洁聚合物压裂液研究与现场应用杜 涛, 姚奕明, 蒋廷学, 陈 作, 张旭东(中国石油化工股份有限公司石油工程技术研究院页岩油气富集机理与有效开发国家重点实验室,北京100101)摘 要:清洁聚合物压裂液是目前国内外压裂液研究领域的热点之一。

以增稠剂(SRFP-1)、交联剂(SRFC-1)、黏土稳定剂(SRCS-1)和助排剂(SRCU-1)工业品作为研究对象,以现场配液用水配制清洁聚合物(SRFP)压裂液,评价了SRFP清洁聚合物压裂液的变剪切性能、破胶性能及压裂液滤液对岩心的伤害性能;测定了破胶液的表面张力。

结果表明:该压裂液在90℃条件下具有良好的耐剪切性能;在60~80℃,破胶剂加入量为0.005%~0.04%条件下,2h即可破胶,破胶液黏度小于5mPa·s,破胶液表面张力小于28mN/m;压裂液滤液对岩心基质伤害率为18.7%;最后将该压裂液成功应用于鄂尔多斯盆地某重点水平井的压裂作业。

关键词:清洁聚合物压裂液;变剪切性能;破胶性能;岩心基质伤害率;现场应用中图分类号:TE357.12 文献标志码:A文章编号:0367-6358(2016)06-0334-04Study on Properties of Clean Polymer Fracturing Fluid and Field ApplicationDU Tao, YAO Yi-ming, JIANG Ting-xue, CHEN Zuo, ZHANG Xu-dong(Sinopec Research Institute of Petroleum Engineering,State Key Laboratory of Shale Oil and Gas EnrichmentMechanisms and Effective Development,Sinopec,Beijing 100101,China)Abstract:Clean polymer fracturing fluid is one of the hot research fields home and abroad.gelling agent(SRFP-1),cross-linker(SRFC-1),clay stabilizer(SRCS-1)and cleanup additive(SRCU-1)were the tar-get objects.Clean polymer fracturing fluid(SRFP)was prepared using the field water.Variable shear per-formance,viscosity break performance and the effects of fracturing fluid on permeability damage of corewere tested.The surface tension of gel breaking liquid was measured.The fracturing fluid showed bettershearing resistance performance under the conditions of 90℃.Under the conditions of 60~80℃,0.005%~0.04%breaker and 2h,the viscosity of the gel breaking liquid was less than 5mPa·s,and thesurface tension of the gel breaking liquid was less than 28mN/m.The permeability damage rate of corematrix caused by SRFP was 18.7%.Finally,the fracturing fluid was successfully used for the fracture ofone key horizontal well in Ordos Basin.Key words:clean polymer fracturing fluid;variable shear performance;gel breaking performance;permea-bility damage rate of core matrix;field application收稿日期:2015-10-12;修回日期:2016-03-17基金项目:国家重大科技专项“大型油气田及煤层气开发—复杂地层储层改造关键技术”(合同编号:2011ZX05031-004-003)资助;中国石化石油工程技术服务有限公司重点项目“合成聚合物压裂液开发与应用”(合同编号:10010099-13-ZC0607-0037)资助;国家自然科学基金重大项目“页岩地层动态随机裂缝控制机理与无水压裂理论”(合同编号:51490653)资助;中国石化科技攻关项目“LPG无水压裂液研究”资助;中国石化科技部院控项目“抗盐压裂液研制”资助;国家重大科技专项“彭水地区高效钻井及压裂工程工艺优化技术”(合同编号:2016ZX05061-002)资助。

清洁压裂液的研究与应用

清洁压裂液的研究与应用
粘弹性是影响粘弹性表面活性剂溶液应用性能的一个最重要的性能指标,很 多学者认为:粘弹性的形成是由于粘弹性表面活性剂在盐水溶液中形成了棒状胶 束,随着棒状胶束的增多而发生了相互缠结,形成了类似交联聚合物大分子的空 间网状结构。
随着粘弹性流体的出现,应用常规评价流体的方法来评价粘弹性流体就碰到 了困难。通过多年的研究,获得了较好的评价方法,即通过应用储能模量(’) 和耗能模量(”)来量度:储能模量是体系弹性效应的量度,而耗能模量则是粘 性效应的量度。同时还可以应用 tgδ 来表征溶液粘弹性的大小。
4.3 粘弹性
粘弹性是 VES 溶液的一个特殊性质。它是一种能在很多胶态体系尤其是很 多表面活性剂溶液中观察到的现象。通过简单的使溶液涡旋和观察捕集在样品中 空气泡的弹性碰撞,很容易发现溶液的粘弹性,VES 溶液在剪切下,不仅会产 生切向应力,同时还会产生法向应力,众多学者研究发现,法向应力的产生是溶 液弹性作用的结果。
3
清洁压裂液的研究与应用
4 清洁压裂液的流变特性
4.1 低粘度特性
在压裂施工中,即使其在很低粘度下(≤20mPa·s)也能对支撑剂达到悬浮稳 定作用,这一性质是聚合物无法比拟的。较低的粘度使其可以有较低的摩阻和低 泵注压力,避免了使用大功率的设备。
4.2 优良的剪切稀释特性
清洁压裂液是由表面活性剂胶束缠结而产生粘弹性,此结构在剪切作用下会 发生拆散,使缠结的胶束团重新转变为单个或较少胶束缠结结构,使粘度大幅下 降,当剪切消失,结构又自动恢复。由于这种特殊的性质,使其广泛应用在油田 开采作业和涂料等领域。
图 5-1 棒状胶束相互缠绕形成的网状结构示意图
5.2 抗剪切机理
清洁压裂液中不含任何高分子聚合物,其粘度是通过表面活性剂胶束的相互 缠绕而形成的,这与胍胶压裂液的粘度形成机理不一样。VES胶束的形成和相互 缠绕是表面活性剂分子之间和表面活性剂聚集体之间的行为,表现为清洁压裂液 的表观粘度不随时间变化以及通过高剪切后体系的粘度又能得到恢复[17],而植 物胶压裂液不耐剪切,分子链的断开会使植物胶的粘度永久地丧失。

清洁压裂液的研究与应用进展

清洁压裂液的研究与应用进展

清洁压裂液的研究与应用进展发表时间:2020-04-15T04:14:59.122Z 来源:《建设者》2020年1期作者:胡晓鹏[导读] 本文首先综述了清洁压裂液的概况及其三种基本机理,其次对国内外的研究现状进行了简述,最后从目前的发展状况出发提出了几点清洁压裂液的发展趋势。

中石化中原石油工程有限公司井下特种作业公司河南濮阳 457000摘要:基于传统聚合物压裂液上提出的黏弹性表面活性剂(VES)压裂液(又名清洁压裂液)中可形成球形胶束,进而演变成具有高黏弹性的空间网状结构,从而实现对支撑剂的有效携带。

清洁压裂液无残余物,不会堵塞地层裂缝,返排性能强,提高了裂缝的导流能力,降低了对地层的损害和污染,增产效果显著。

本文首先综述了清洁压裂液的概况及其三种基本机理,其次对国内外的研究现状进行了简述,最后从目前的发展状况出发提出了几点清洁压裂液的发展趋势。

关键词:清洁压裂液;黏弹性表面活性剂;机理;发展现状水力压裂技术作为提高油气层产率的有效办法,在油气井增产、水井增注、提高低渗透率方面发挥了巨大的作用。

新型清洁压裂液具有残渣少、耐高温、黏度高、返排性好,同时又具有破胶迅速携砂能力强、降滤失性能优等特点。

在压裂作业时能够在目的储层形成一条具有优良导流能力的缝隙,油气储层的渗透性得到很大的提升,不仅可以有效地提高油气井的采收率,还减少了流体在地层裂缝中的渗透阻力和对油气储层的岩心伤害,达到了油井增产和注水增注的目的,从而受到人们的广泛关注,展现出良好的应用前景。

1 清洁压裂液的作用机理成胶机理黏弹性表面活性剂分子中含有亲水基和疏水基,分子链上有正负电荷。

在纯水中,亲水基伸入水相,长链疏水端远离,形成长链疏水基包裹的低黏度球形胶束。

加入盐或反离子表面活性剂等对胶束和水之间的电荷进行屏蔽,占有空间变小,胶束间通过范德华力和弱化学键的作用互相缠绕,转变为柔性棒状胶束。

随着浓度不断增加,在疏水基作用下胶束之间自动进行纠缠,形成空间网络结构。

国内清洁压裂液的研究与应用

国内清洁压裂液的研究与应用

国内清洁压裂液的研究与应用一、介绍国内清洁压裂液的研究背景和现状1. 压裂技术的作用和发展历程2. 清洁压裂液的重要性和发展趋势3. 国内清洁压裂液的研究现状二、清洁压裂液的组成及性能要求1. 清洁压裂液的组成成分2. 清洁压裂液的性能要求3. 相关管控规范三、清洁压裂液的制备工艺1. 传统压裂液的制备2. 清洁压裂液的制备方法和工艺3. 清洁压裂液的配方设计和优化四、清洁压裂液在页岩气开发中的应用进展1. 清洁压裂液在页岩气开发中的优势和应用前景2. 清洁压裂液在国内页岩气开发中的应用现状3. 清洁压裂液在页岩气井生产中的应用效果五、清洁压裂液的未来发展方向和建议1. 清洁压裂液研究的挑战和机遇2. 清洁压裂液的未来发展方向3. 政策建议和技术创新的推广措施注:以上提纲只作参考,具体论文撰写需要根据实际情况进行调整和优化。

压裂技术作为一种提高页岩气开采率的重要技术手段,在页岩气勘探和开发中得到了广泛应用。

随着页岩气产业的发展,越来越多的人关注到了压裂液的环保性和经济性问题。

为了避免污染环境和降低成本,国内开始加大清洁压裂液的研究和应用力度。

压裂技术的作用和发展历程:压裂是一种通过高压液体将石油、天然气等油藏内的裂隙扩大、连接起来,以提高油气开采率的工艺。

自1947年以来,压裂技术经历了长足的发展。

在过去的几十年里,压裂技术已经由浅部压裂发展成为深部压裂、多点压裂和水力喷射等多种技术方法,取得了重大的石油、天然气和地热能开采成果,并成为油气勘探和开发的重要技术手段之一。

清洁压裂液的重要性和发展趋势:随着页岩气开发的快速发展,压裂液的质量成为页岩气开发的一个重要问题。

传统压裂液存在环境污染和经济问题,如井下回收、长距离运输和废液处理等方面都存在一定的问题。

为了缓解这些问题,清洁压裂液逐渐成为了压裂液技术的一个热点问题。

清洁压裂液具有环保、经济、稳定等优点,因此在页岩气开发中的应用前景广阔,这也是为什么越来越多的国内研究机构和公司开始加大清洁压裂液的研究和应用力度。

新型压裂技术的研究和应用

新型压裂技术的研究和应用

新型压裂技术的研究和应用第一章介绍近年来,随着全球需求的增加,石油天然气行业的需求也在增加。

为了满足这一需求,需要采取一些新技术。

其中最受关注的新技术之一是新型压裂技术。

本文将探讨新型压裂技术的研究和应用。

第二章压裂技术压裂技术也被称为水力压裂技术。

它是一种通过将液体注入到地下岩石中来刺激地下岩石中的天然气或石油流动的技术。

通常使用水和一些化学药品混合物作为液体。

这些药品旨在减少液体黏性并保持岩石孔隙中的水能够流动。

第三章压裂技术的发展压裂技术最初在1947年被发明。

在这个时间点之前,只有传统的岩石破坏技术和油井摇杆技术可用于开采油气资源。

然而,压裂技术很快被证明是一种更有效的技术,可以更容易地开采地下的油气资源。

随着时间的推移,压裂技术也在不断改进。

新的压裂技术在液体注入、混合物、泵的尺寸和压力方面有所不同。

这些新技术使压裂更有效,也更环保和更安全。

尽管传统压裂技术在近些年来广泛应用,并得到了改进,但是仍然存在一些问题。

下面是一些主要问题:(1)使用的化学药品可以导致对环境的污染(2)高压泵可能导致地震的发生(3)在压裂过程中建造新的水井会增加地下水污染的风险第五章新型压裂技术为了解决传统压裂技术的问题,一些新型压裂技术已被开发出来。

下面介绍一些新型压裂技术:(1)超临界流体压裂技术超临界流体压裂技术是一种新型的压裂技术。

它使用超临界流体代替传统的水和化学药品混合物。

这种技术不会对环境造成污染,并且可以减少压裂需要的水量。

此外,超临界流体压裂技术也更安全,不会导致地震的发生。

(2)微尺度裂缝压裂技术微尺度裂缝压裂技术是一种基于纳米技术的新型压裂技术。

它使用微米级别的裂纹来刺激地下岩石中的油气流动。

使用这种技术不会对环境造成负面影响,并且建造新的水井的需求也大大减少。

新型压裂技术已经在全球范围内得到了广泛应用。

下面介绍一些应用案例:(1)美国德州的巴尔布特气田巴尔布特气田位于德州北部。

在过去几年中,废水处理工厂开始使用超临界流体压裂技术来管理他们的固体废物。

国外清洁压裂液的研究进展_陈馥

国外清洁压裂液的研究进展_陈馥

文章编号:1000-2634(2002)05-0065-03国外清洁压裂液的研究进展Ξ陈馥1,王安培2,李凤霞2,李兴应2(1.西南石油学院化学工程系,四川南充637001;2.中原油田分公司采油工程研究院)摘要:粘弹性表面活性剂(V ES)基压裂液(又称为清洁压裂液(ClearFRAC))的使用改变了传统聚合物压裂液对支撑剂的输送方式,可以消除残余聚合物对支撑剂充填层的堵塞,并能提高充填层的导流能力。

总结和回顾了目前国内现有的压裂液体系及存在的问题,对国外清洁压裂液的研究状况、理论基础、研究进展及井场应用情况进行了综述。

井场应用结果及与瓜胶压裂液体系组分对比表明:清洁压裂液性能优于聚合物压裂液,具有高效、低伤害、配制简单的特点。

最后对目前我国开展清洁压裂液的研究提出了一些建议。

关键词:压裂液;清洁压裂液;压裂添加剂;储层保护中图分类号:TE254.4 文献标识码:A1 压裂液技术发展简述压裂作为油气藏的主要增产、增注措施已得到迅速发展和广泛应用,压裂液是压裂技术的重要组成部分。

目前,国内外最常使用的压裂液为水基压裂液,其大致可分为3种类型:[1](1)天然植物胶压裂液;(2)纤维素压裂液;(3)合成聚合物压裂液。

随着水力压裂技术的进步,为使支撑剂远离井眼达到深穿透,国外从60年代末就开始使用高粘度的交联压裂液。

交联压裂液的发展,保证了高温深层压裂施工的成功。

但是如果压裂液在地面交联,施工时以高速进入管线和通过炮眼,高速剪切仍然会造成严重的剪切降解,产生永久的粘度损失。

因此,在80年代,水基压裂液一个显著的发展是采用了延迟交联技术。

这使得压裂液可产生较高的井下最终粘度和更好的施工效率。

上述几种压裂液体系,已在国内外各油田得到广泛的应用,并取得良好的增产效果。

但使用这些压裂液体系的共同的缺陷,就是压裂液破胶不完全,而且破胶后残渣将残留在裂缝内,残留在裂缝中的聚合物将严重的降低支撑剂充填层的渗透率,从而伤害产层,导致压裂效果变差。

无伤害压裂液流变模式研究

无伤害压裂液流变模式研究

无伤害压裂液流变模式研究第1章概述1.1 本论文的研究意义压裂液是压裂工艺技术的一个重要组成部分。

其主要功能是造缝并沿张开的裂缝输送支撑剂,因此液体的粘性至关重要。

然而,成功的压裂作业还要求液体具备其他的特殊性能,除在裂缝中具有要求的粘度外,还要能够破胶,作业后能够迅速返排,能够很好地控制液体滤失,泵送期间摩阻较低,同时还要经济可行。

为了更大限度的发现油气藏、保护油气层产能,提高油田产量,实现油田的宏伟目标,项目的研究开发具有更大的现实意义,为了赶超世界石油开发的先进技术水平,限制一些国家垄断,为大庆油田[2]的“稳油控水”降低原油的开采成本,项目开发具有一定的政治意义和巨大的经济效益。

1.2 压裂液添加剂的现状及展望1.2.1胶凝剂1.2.1.1国外状况国外90年代应用的胶凝剂仍以胍胶及其衍生物和纤维素[3]及其衍生物为主。

胍胶有未改性的天然胍胶、羟丙基胍胶(HPG)、羧甲基羟丙基胍胶(MHPG)、羧甲基羟乙基胍胶(MHEG)等。

纤维素有羧甲基纤维素、羧甲基羟乙基纤维素、羧甲基羟丙基纤维素及羟乙基纤维素等。

但应用最多的是胍胶类,占总用量的90%。

据统计,世界六大油田化学剂公司产品中以上两大类胶凝剂有103种产品。

(1)半乳甘露聚糖胶凝剂硼交联的胍胶凝液是一种改良组分,可用于135~148℃高温井压裂。

它的高温稳定性主要依赖于含有的MgO和氟离子。

氟离子的作用是防止MgO在高温下沉淀,来源于KF、NH4F、NH4HF2。

适用于地层温度低于160℃的油气井压裂。

胍胶或具有10万分子量的羧甲基羟丙基胍胶0.2%~1.25%、水20%~100%、pH值维持2~4.4的缓冲液、交联剂-羧酸铝和醋酸及铝螯合剂、缓交联剂等组分组成的压裂液具有足够长的缓交联时间供施工作业,并具有较好的携砂能力。

用多糖或纤维素衍生物胶凝剂配制压裂液的组分为:①含钾离子的水基液;②以半乳甘露聚糖及其改性产品或衍生物和纤维素衍生物作为胶凝剂;③交联剂;④选自碱金属氯化物及次氯酸盐的足量破胶剂;破胶剂的活化剂,一种含有铵离子或能产生铵离子的化合物。

压裂液调研报告

压裂液调研报告

压裂液的研究进展调研报告压裂已经广泛应用于增产当中,压裂液的性能在作业中起到至关重要的作用。

压裂液存在着破胶难,污染环境,污染储层,抗温抗盐性能差的问题。

为此,在研究大量文献的基础上,回顾了压裂液技术的发展和现状,总结了适合不同地层条件的国内外压裂液新技术,以及现阶段存在的问题,展望了未来的发展方向。

研究结果表明,目前仍是以聚合物增黏剂为主的水基体系,并且研究出了抗高温清洁压裂液,微束聚合物压裂液,无聚合物压裂液以及新型原油基压裂液等等。

水基压裂液残液五步处理法,在现场应用效果明显,残渣,破胶性能,相容性,水锁伤害是储层伤害的主要原因。

压裂液将主要朝着地层伤害小,抗温抗盐,地层适应性强,环境友好的方向发展。

压裂液的类型:水基压裂液、油基压裂液、酸基压裂液、泡沫压裂液。

压裂液自从1947年首次用于裂缝增产以来经历了巨大的演变。

早期的压裂液是向汽油中添加足以压开和延伸裂缝的黏性流体;后来,随着井深的增加和井温的升高,对压裂液的黏度提出了更高的要求,开始采用瓜胶及其衍生物基压裂液。

为了在高温储层中达到足够的黏度和提高其高温稳定性,研究出了高温油基压裂液。

最初使用的压裂液是炼制油和原油,由于最初担心压裂液和含有非酸性水液的油气储层接触,可能产生不利影响,后来实验已经证明,用适当的添加剂(粘土控制物质,表面活性剂等),使用水基液能处理大部分油气储层,在一个已知储层的压裂液处理中,最好是通过实验室地层岩心实验(或者一贯的现场结果)来确定水基压裂液的可用性。

水基压裂液体系及技术包括:非交联型黄原胶/魔芋胶水基冻胶压裂液技术、pac阳离子聚合物压裂液体系、有机硼交联水基压裂液技术、哈利伯顿微束聚合物压裂液体系、高黏度水基压裂液、无聚合物压裂液体系、低凝胶硼酸压裂液、无固相压裂液、无破胶剂压裂液技术压裂液。

油基压裂液体系及技术:低渗、低压、水敏性油气藏储量占每年探明储量的1/3而且有继续上升的趋势,有效合理地开发这部分油气藏对稳定增加油气产量意义重大。

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№.5 陕西科技大学学报 Oct.2008 Vol.26 J OURNAL OF SHAANXI UN IV ERSIT Y OF SCIENCE&TECHNOLO GY ・33・3 文章编号:100025811(2008)0520033206STU DY AN D APPL ICATION OF NON2DAMAGINGFRACTURING FL UIDL I Lin2di,ZHAN G Shi2cheng,ZHAN G Jin(MO E Key Laboratory of Petroleum Engineering in China University of Petroleum,Beijing 102249,China)Abstract:As an external fluid,f ract uring fluid harms formation in various extent s.There2fore,decreasing t he damage is t he prerequisite to imp roving f ract uring stimulation effect andis t he developing t rend of fract uring fluid.Non2damaging f ract uring fluid is an anionic cleanf ract uring fluid which integrates t he characteristics of visco2elastic behavior and anti2shearingand automatic viscosity breaking.It has great advantages such as easy manufact uring,fewadditives,having no residues and little damage.The field applications indicate t hat non2dam2aging fract uring fluid breaks viscosity easily and has low const ructing frictions and st rongcarrying capacity and cont rols f ract ure height effectively.Agreeable field applications showpromising f ut ure of non2damaging f ract uring fluid.K ey w ords:non2damaging;clean f ract uring fluid;anio nic surfactant;evaluation of perform2ance;field applicationsC LC Number:TE357.1+2 Document Code:A0 IntroductionAs an extensively applied contemporary engineering,hydraulic f ract uring has a very p romising f u2 t ure in various fields such as oil p roduction and coal formatio n flooding and eart h st ress measurement and reservoir induced seismicity and dam and side slope destabilizing co nt rol and geot hermal exploitation[1]. Hydraulic f ract uring has been becoming one of t he most important stimulation met hods for t he develop2 ment of low2permeability reservoir where oil production has been greatly advanced by imp roving t he fil2 tering flow co nditions nearby bottom hole.For example,more t han30%crude outp ut in American is obtained by hydraulic f ract uring[2].Fract uring fluid is an essential component part of hydraulic f ract uring project and plays an important role on t he const ructio n work and f ract ure geomet ric shape and f ract uring effect.One of t he mo st valua2 ble index marks to weigh t he f ract uring fluid is t he extent of it s damage to t he formation and t he p ropped f ract ure[3].After years of hard work,non2damaging f ract uring fluid is successf ully developed.This pa2 per st udied it s formula optimization and evaluation of performance.The experiment s indicated t hat non2 damaging f ract uring fluid was manufact ured simply and used few additives and had no residues and broke visco sity easily and had st rong carrying capacity.Moreover,t he field applications gained agreeable re2 sult s.3收稿日期:2008206224作者简介:李林地(1980-),女,河南省南阳市人,在读博士生,研究方向:油气井增产技术基金项目:国家重大课题专项《低渗透油田储层保护与油藏整体压裂改造技术研究》(2007BAB17B03)资助陕西科技大学学报第26卷1 MechanismHydraulic f ract uring is an operation which uses high2pressure p ump group on t he eart h surface to p ump high visco sity f ract uring fluid into well bore at t he delivery rate exceeding t he formation absorba2 bility.Thus,high p ressure will be caused in t he bottom hole.And when it overcomes t he eart h st ress nearby borehole face and reaches t he rock tensile st rengt h,t he f ract ure will be created and will extend forward.In order to avoid t he f ract ure closing after t he high pressure fluid′s flowback,t he carrying fluid is p umped afterwards to extend t he fract ure continuously and to send t he p roppant to t he fract ure.After t hat,high visco sity fluid is broken into low visco sity to ret urn to t he well and t hen flowback to t he eart h surface.As a result,a high conductivity f ract ure remains in t he layer and it is beneficial for oil and gas flow into t he well f rom far distance[4].The main f unctions of f ract uring fluid are creating f ract ure and t ransporting proppant to t he wide2 open fract ure.At p resent,t he most general p urpo se fluid is water soluble polymers wit h cross2linking f ract uring fluid[5].Alt hough it has great sand carrying capacity,t he macromolecules might be adsorbed and left in t he formation pore,which could cause damage to reservoir.Simultaneously,visco sity break2 ing is inadequate and t hen t he residues would seriously decline t he permeability of proppant bed deposi2 tion[6].Schlumberger developed t he visco2elastic surfactant f ract uring fluid(VSE)in1997which is characterized as low f riction and high sand carrying capacity and wit hout solid residues and so on.Thus it has been imp roved quickly in t he past few years[7210].However,t he first generation VSE fluid is cat2 ionic surfactant,while sandstone surface is usually carrying negative elect ricity,so VSE fluid is likely to be adsorbed on sandsto ne surface and it may revise t he wettability and decrease t he size of pore t hroat. Thereby,t he permeability of t he formation nearby f ract ures would be declined.Recently more and more attention is attracted on t hese problems[11].Non2damaging fract uring fluid is an anio nic clean f ract uring fluid which not only inherit s t he advan2 tages of t he first generation V ES fluid but also could avoid t he adsorption on sandstone surface.In a word,it is harmless for t he formatio n and t he p ropped fract ure.2 Formula Optimization ExperimentsAnionic surfactant D3F2AS05is optimized as t he f undamental agent of non2damaging fract uring flu2 id.Besides,KCl and ED TA are chosen as t he anti2swelling agent and t he anti2precipitant.The amount of every co mponent plays a great role on t he performance of non2damaging f ract uring fluid.Formula op2 timization experiment s are shown as following.2.1 Formula ratio of ED TABlend t he formation water from some gas field(degree of mineralization67519.03mg/L,SO422 0.27mg/L,Ca2+12265.28mg/L,Mg2+208.54mg/L)and t he f ract uring fluid(3.0%D3F2AS05+ 6%KCl+0.5%KO H)wit h t he volume ratio of1∶1,t hen add different quantitative ED TA.The ap2 pearances of t he blend fluids are shown as Tab.1.The fluid could prevent t he formation water from scal2 ing if t he amount of ED TA is above0.3%.2.2 Formula ratio of KClT ab.1 Optimization of the amount of E DTAThe amount of ED TA0.1%0.2%0.3%0.4%The appearance of the blend fluid White cloudedfluidMilky whitesemi2opaqueAchromatictransparentAchromatictransparentOn t he basis of t he formula3.0%D3F2AS05+0.3%ED TA+0.5%KO H,consider t he influenceof t he amount of KCl on t he vis2・43・第5期李林地等:无伤害压裂液的研究与应用co sity of t he fract uring fluid.Fig.1shows t hat t he concent ration of KCl in t he system should be be 2tween 6%and 8%.Generally ,t he concent ration of KCl as anti 2swelling agent in t he f ract uring fluid is about 2%.So according to t he work 2load of dispending fluid ,it is better to choo se 6%KCl.Fig.1 The curve of the amount of K Cl influencing Fig.2 The curve of the amount of D3F 2AS05on the viscosity of non 2damaging fracturing influencing on the viscosity of non 2fluid damaging fracturing fluid2.3 Formula ratio of D3F 2AS05On t he basis of t he formula 6%KCl +0.5%KO H +0.3%ED TA ,change t he mass concent ration of D3F 2AS05.Fig.2shows t he visco sity 2temperat ure curves of t he f ract uring fluid.The larger t he mass concentration of D3F 2AS05is ,t he higher capability of it s anti 2temperat ure is.In order to meet t he de 2mand of sand carrying ,t he visco sity of t he f ract uring fluid should be larger 30mPa ・s under 170s 21.So 3%D3F 2AS05is reasonable.Finally ,t he optimized formula of non 2damaging f ract uring fluid is 3.0%D3F 2AS05+0.3%ED TA +6%KCl +0.5%KO H and it s visco sity is 40mPa ・s under air temperat ure and 170s 21.3 Evaluation of PerformanceAdopt oil and nat ural gas professional criterion S Y/T 510721995“The met hod of evaluation of per 2formance of aqueous fract uring fluid ”to do some experiment s to evaluate t he performance of non 2dama 2ging f ract uring fluid such as temperat ure tolerance and anti 2shearing and visco sity breaking and sand car 2rying capability and t he damage to t he formation.3.1 Visco sity 2temperat ure characteristics and anti 2shearing performanceEvaluate t he viscosity 2temperat ure characteristics and t he anti 2shearing performance of non 2dama 2ging f ract uring fluid by means of HA KER visco simeter.It could be seen t hat t here is a high viscosity point at 115℃in Fig.3,so t he optimum temperat ure is between 100℃and 120℃.Fig.4shows t hat t he fluid has a st rong anti 2shearing performance (170s 21).At first t he visco sity drop s because of t he vis 2co sity 2temperat ure effect ,but it maintains steady 20minutes later.3.2 Visco sity breakingperformanceFig.3 The viscosity 2temperature curve of Fig.4 The anti 2shearing perform ance curve ofnon 2dam aging fracturing fluid non 2damaging fracturing fluid・53・陕西科技大学学报第26卷Non 2damaging fract uring fluid could break visco sity by contacting wit h crude oil or diluting forma 2tion water.Blend non 2damaging f ract uring fluid and reagent wit h t he volume ratio of 1∶1,stir t hem at a high speed about one minute and keep t he mixt ure under a constant temperat ure.As shown Tab.2,t he result s indicate t hat non 2damaging fract uring fluid would break visco sity (viscosity is below 5mPa ・s )if it contact s crude oil only one hour later.While wit h formation water (using t he normal saline in t he experiment ,t he compo nent is 70000pp m NaCl +6000pp m CaCl 2+4000pp m MgCl 2)t he viscosity breaking is slower because dilution requires more formation water.The compatibility of non 2damaging f ract uring fluid and t he formation water is good and t here are no residues.Additionally ,non 2damaging f ract uring fluid breaks easily wit h f resh water (tap water ).T ab.2 The viscosity breaking performance ofnon 2damaging fracturing fluidReagentViscosity bre 2ak time/h 40℃viscosity /mPa ・s 80℃viscosity /mPa ・s Crude oil1125Formation water2.52516Fresh water 1.51793.3 Proppant carrying capacity Sufficiently blend 50g ceramsite wit h t he density of 3.31g/cm 3and 100mL non 2damaging fract uring fluid ,and proppant is still suspended after being mixed and kept intact 16h.It shows t hat non 2damaging fract uring fluid has a st rong proppant carry 2ing capacity and it is advantageous to brace t he fract ure evenly after it is clo sed.3.4 Damage experimentConfer oil and nat ural gas professional criterion S Y/T 510722005“t he met hod of evaluation of per 2formance of aqueous fract uring fluid ”to do t he experiment of damage to core at 80℃.The cores come f rom Neopaleozoic reservoir in a gas field.The grain grade gives priority to medium and coarse grain.The content of quartz is between 67%and 90.5%and t he range of feldspar is 0.7%~3.8%.Major li 2t hologic character is lit hic sandstone and lit hic quartz sandsto ne and quartz sandstone.The absolute co n 2tent of clay mineral is very low (≤5.37%).Chief clay mineral is goeschwitzite and kaolinite but wit hout mont morillonite.The content of kaolinite is high (average value is 58.2%).And it is occurred in t he form of inter 2granular filled gat hering but t he disperse state is seldom seen.BXHP G is t he boron cro ss 2linking guanidine f ract uring fluid who se principal ingredient s are 1%KCl +0.45%H P G +0.2%clean up additive DL 210+1%YFP 21foaming agent +0.1%met hanal +0.2%Na 2CO 3+0.05%ammonium persulfate +0.3%cro ss 2linker BCL 261A +20%NaO H.The domi 2nant ingredient of HP G linear gel are 0.3%HP G +1%KCl +0.2%clean up additive +0.1%met hanal +1%foaming agent +0.1%ammonium persulfate.The essential constit uent s of t he first generation V ES fract uring fluid are 3.0%cationic surfactant +2.5%KCl.Tab.3shows t hat non 2damaging f ract u 2ring fluid is nearly harmless to t he core.T ab.3 The damage experiment with different fracturing fluidsFracturingfluidNo.core Core length /cm G as survey permeability /1023μm 2Water survey permeability /1023μm 2Injection rate /PV Water survey permeability after injection /1023μm 2Damage /%BXHP GD4722 5.710.1740.022210.014435.1HP GD4725 6.80.1510.0225 2.50.014933.9V ESD4726 3.780.1190.0213100.018214.6Non 2damaging D47236.730.130.0248100.0244 1.63.5 Visco 2elastic behavior・63・第5期李林地等:无伤害压裂液的研究与应用In fact ,f ract uring fluid is a visco 2elastic fluid.The modulus of energy storage G ′is used to measure t he shearing energy in t he elastic fluid when shearing stress exsites.So G ′is t he yardstick to measure t he elasticity.The modulus of att rition G ″is used to measure t he t hermal energy which is t ranfromed by viscous flowing.So G ″is t he yardstick to measure t he viscosity [12].The weaker t he elasticity is ,t he weaker proppant carrying capacity is.But t he higher t he viscosity is ,t he higher t he f riction is.The re 2search shows t hat it is reasonable to apply G ′/G ″to evaluate t he visco 2elastic behavior of fract uring flu 2id.The best fract uring fluid is one wit h low visco sity and high elasticity.Tab.4shows t hat non 2dama 2ging f ract uring fluid is indeed an excellent fluid. T ab.4 The comparison of visco 2elastic be 2havior of different fracturing fluids (The ex 2perimental temperature is 90℃and the os 2cillation frequency is 0.1~10H z)Fracturing fluidG ′/Pa G ″/Pa G ′/G ″BXHP G0.80.42V ES8.50.2830.4Non 2damaging 9.80.2539.24 Field Application and ConclusionNon 2damaging f ract uring fluid showed agreeable qualities when it was applied in Daqing Oil Field and Dani 2udi Gas Field and Henan Oil field.For instance ,t he per 2forated intervals of a well in Daqing Oil Field were 2042.6~2040.2m ,2006.6~2003.0m ,1982.2~1980.6m and 1978.621976.2m.It was f ract ured bylayering and back 2reaming.The formation temperat ure was 85℃and viscosity breaker was not used during t he fract uring.Bean up after shutting t he well 3hours ,t he visco sity was broken completely and flow 2back ratio was up to 95%.The p roduction was imp roved from 1t/d to 13.2t/d t hrough t he f ract u 2ring t reat ment using non 2damaging f ract uring fluid.From t he result s of t he f ract uring simulation and well temperat ure test after f ract uring ,it could be seen t hat fract ure height was cont rolled effectively and t he lengt h was eno ugh and it was nearly harmless ,so it was beneficial to broaden oil and gas drainage area and to keep t he production plateau long.Non 2damaging fract uring fluid breaks visco sity co mpletely and has no residues and has strong anti 2shearing capability and good temperat ure tolerance.It also has an excellent proppant carrying capability and low f riction and nearly harmless.Filt ration p roperty is also controlled well and t he capability of flow 2back is excellent.High quality and low damage is t he developing t rend of t he f ract uring fluid.Non 2damaging f ract u 2ring fluid could improve f ract ure flow conductivity and accomplish nearly paring t he water soluble polymers wit h cross 2linking fract uring fluid and t he first generation V ES f ract uring fluid ,non 2damaging f ract uring fluid has a very p romising f ut ure.R eferences[1]J.L.G idley.New Development of t he Techniques of Hydraulic Fracturing[M ].Beijing :Petroleum Industry Press ,2002.[2]J.Shyapobersky ,A.Chudnovsky.Review of recent development in fracture mechanics wit h petroleum engineering applications[C].SPE ,1994:28074.[3]L U Y ong 2jun.Recent advances of 90′s foreign fracturing fluid technology[J ].Chemical Engineering of Oil and Gas ,1998,27(2):1152118.[4]ZHAN G Qi.Theory and Design of Petroleum Engineering[M ].Dongying :University of Petroleum Press ,2000.[5]M.J.Economides.Reservoir Stimulation (Third Edition )[M ].Beijing :Petroleum Industry Press ,2002.[6]WAN G Guo 2lu ,J U Quan 2yi.The damage of water 2based cross 2linked gel fracturing fluid to sandstone formation [J ].OilfieldChemistry ,1986,(3):1492158.[7]G ino Di Lullo ,Atikah bte Ahmad ,Phil Rae ,et al .Toward Zero Damage :New Fluid Point s t he Way[C].SPE ,2001:69453.[8]Mat hew Samuel ,Dan Polson ,Don Graham ,et al .Visco 2elastic Surfactant Fracturing Fluids :applications in low permeability res 2・73・陕西科技大学学报第26卷ervoirs[C].SPE ,2000:60322.[9]Chase B ,Cheilowski W ,Marcinew R ,et al .Clear fracturing fluids for increased well productivity[J ].Oilfield Review ,1997,9(3):20233.[10]L IU Xin 2quan ,YI Ming 2xin ,ZHAO Jin 2ju ,et al .Visco 2elastic surfactant based fracturing fluids[J ].Oilfield Chemistry ,2001,18(3):2732277.[11]CH EN Fu ,L IU Y i ,WAN G Da 2yong.St udies in formation damages caused by cationic surfactant base fracturing fluids[J ].Drill 2ing Fluid &Completion Fluid ,2007,24(6):62265.[12]CON G Lian 2zhu.Preliminary study on t he visco 2elasticity of borate gelling fracturing fluid[J ].Drilling Fluid &Completion Fluid ,1995,12(6):35239.无伤害压裂液的研究与应用李林地,张士诚,张 劲(中国石油大学石油工程教育部重点实验室,北京 102249)摘 要:压裂液作为外来流体进入地层可能会对地层造成不同程度的伤害,减少压裂液对储层的伤害是提高压裂增产效果的重要前提,也是压裂液发展的方向.对压裂液多年研究的基础上,开发成功了无伤害压裂淮,该压裂液是一种阴离子型清洁压裂液,集粘弹性、抗剪切性、自动破胶性于一体,具有配制简便、使用添加剂种类少、不存在残渣、对储层伤害小等特点.现场试验表明,无伤害压裂液易破胶,施工摩阻低,携砂能力强,可有效地控制缝高,压裂施工后增产效果明显,有着广阔的发展前景.关键词:无伤害;清洁压裂液;阴离子表面活性剂;性能评价;现场应用中图分类号:TE357.1+2 文献标识码:A(上接第5页)[9]Valdek Mikli ,Helmo Kaerdi ,Priit K.Characterization of powder particle morphology[J ].Proc.Estonian Acad.Sci.Eng.,2001,7(1):22234.[10]Anne Skriver ,Martin B.Hansen ,Karsten B.Q.Image analysis applied to elect ron micrographs of stirred yogurt [J ].Journal ofDairy Research ,1997,64:1352143.合成纤维成纸横截面SEM 图像量化分析张素风,张美云(陕西科技大学造纸工程学院,陕西西安 710021)摘 要:将Image J 程序应用于合成纤维成纸横截面SEM 图像的量化分析.对随意选取的合成纸横截面的一个SEM 图像计算了纸张z 向结构的纤维直径和纤维形状因子,分析并估算了纸张结构中的孔隙分布和浆料配比.试验采用的试样纸中合成纤维直径范围为14.10~20.38μm ,平均直径为17.37μm ;纤维形状因子为1.57~3.0,平均值为1.97;纸张的孔隙率为11.59%,纸张成形匀度很好,孔隙分布也比较均匀;图片中纸张反映出两种纤维配比为1∶1.研究结果表明使用该方法对同一样品的多张不同图片进行统计分析,可以得到可靠的浆料配比数据.关键词:SEM 图像;合成纤维纸;孔隙分布;纤维直径;纤维配比中图分类号:TS71+.2;TP391.41 文献标识码:A・83・。

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