非常规/复杂油藏

经过多年不断延长的压裂阶段,一些工程师表示,压裂阶段越短越好

压裂设计的趋势是更长的阶段和更多的射孔簇,这节省了时间和金钱。但有几家公司正在测试较短的时间是否更有利于生产。

压裂现场,唐宁公司的两个大型白色装置装有一个自动化系统,该系统在压裂过程中控制泥浆从泵流入井中的流量。
压裂现场,唐宁公司的两个大型白色装置装有一个自动化系统,该系统在压裂过程中控制泥浆从泵流入井中的流量。
资料来源:唐宁。

压裂设计的趋势是更长的阶段和更多的射孔簇,这节省了时间和金钱。

从今年SPE水力压裂技术大会暨展览会上的论文来看,大幅减少单簇射孔数、提高压裂效果的思路正在成为行业常态。

但也有一些公司对这一共识提出质疑,他们通过对更短阶段和更少井群的压裂井来看看是否能带来更多的石油和天然气产量。

康菲石油公司高级工程研究员戴夫·克莱默 (Dave Cramer) 表示,康菲石油公司一直在考虑“向后减少每级集群数量”。

“在一些地区,我们根据补偿井中基于光纤的观察,在每个阶段测试更少的簇,这表明远场处理均匀性因此得到改善,”他说,并补充道,“减少阶段长度是增加水力压裂的注入速率,从而增加裂缝宽度并改善支撑剂输送。”

Devon Energy 最近发表的一篇论文中提到了偏移井观测结果,该论文报告了一项测试,得出的结论是,簇较少的阶段比簇较多的较长阶段的压裂效率更高 ( SPE 212340 )。

这篇 36 页的论文基于Eagle Ford水力压裂试验场 1 的第三阶段的广泛测试,其中每阶段使用各种簇进行压裂,以找到一种最有效地重复压裂生产岩石的方法通过旧的断裂设计。

这些数据与支持与美国能源部建立公私合作伙伴关系的公司共享,其中包括康菲石油公司。

该论文的作者写道,“一般来说,集群较少的阶段设计的集群效率更高。”

簇效率取决于簇中的入口孔以足够高的速率获得足够的流体以产生生产性裂缝。断裂长度是其他选择的结果,包括泵速、入口孔数量、直径和位置。

这些设计背后的思想(当今最破裂的)是基于有限的输入方法。该技术确保泵送速率和流体体积足以正确刺激所有穿孔,这些穿孔的尺寸和位置被确定为确保所有入口孔都有机会形成裂缝。

该行业对均衡治疗的关注可以追溯到使用光纤进行的早期研究,该研究表明,最靠近外侧脚后跟侧的第一个簇吸收了大部分液体并形成了主要裂缝,留下了许多后来的簇受到刺激。

根据德文郡和赫斯最近的论文,有限的进入确保了大多数集群受到刺激,但占主导地位的集群仍然获得超过其份额,因为高流速有利于它们获得更多的流体,也确保它们更快地侵蚀,从而使它们能够吸收更流畅。

德文郡的论文称,“无论预期的设计如何,增产都会形成类似大小的主要裂缝,并消耗类似数量的液体。” 这意味着无论是还有 10 个集群还是 20 个集群需要刺激,后续阶段剩余的流体流量大致相似。

根据德文郡的测试井结果,压裂效率随着每级压裂簇数量的增加而下降。考虑到压裂更多级的成本更高,一些效率损失是可以接受的权衡。但数据表明这是有限度的。

“总(泵送)速率不足以破坏所有 22 个性能。德文郡的地球物理学家杰克逊·哈芬纳 (Jackson Haffener) 在俄克拉荷马城 SPE 石油和天然气研讨会上发表有关该论文的演讲时表示,这限制了您从这些脚趾簇中获得的信息。

在研讨会上,哈芬纳表示,通过新的、更短的阶段设计,“现在留下的资源更少,集群数量更少。”

克莱默表示,较短的阶段和较少的集群所带来的产量收益预计将是“有意义的”。

“我们一直在努力降低成本,”但“我们可能需要多花一点钱才能获得最大的利润,”他补充道。

为什么要这样做?

对于那些考虑尝试使用更少集群的较短阶段的完井工程师来说,这些鼓舞人心的话语无法回答一个明显的问题:较短的阶段可以生产多少?

上述引述表明较短的阶段可以输送更多的石油和天然气。但根据已披露的信息,几乎没有公开信息表明缩短时间是否可以增加所需的产量,以证明压裂更多阶段的成本是合理的。随着上市公司扩大主要股票的份额,这一点变得至关重要。

Rystad 页岩油供应链研究副总裁 Justin Mayorga 表示:“如果他们花更多的钱,就会有很大的动力去了解原因。”

企业愿意投入更多资金的领域是行之有效的增加产量的方法;例如,他说,公司正在抽出更多的沙子,二叠纪盆地的平均沙子从每英尺 2,200 磅上升到每英尺 2,500 磅。他补充说,这反映了沙子产量的反弹,这使得价格降至可以承受的水平。

马约尔加表示,公司还在超高马力泵上投入更多资金,这样可以更有效地提供有效压裂多口井所需的抽水量,并逐步淘汰柴油动力泵,转而使用成本较低的天然气泵。 。

他们在多轮诊断测试和分析上投入更多资金,以找出设计油井时最有效的选择。

一个很好的例子是 Hess 用于证明纳入其当前设计标准的想法的过程,该过程在一篇论文中进行了描述,其中标题将其新集群设计称为“一击奇迹”(SPE 212358)。

对于 SPE 现场测试报告来说,这是一个引人注目的标题,它支持了一次性集群的价值。但经过进一步考虑,赫斯的团队担心读者可能会将这句话与“单打奇迹”的歌曲联系起来,这与其系统性的长期绩效改进计划背道而驰。

该论文描述了赫斯改变巴肯压裂方法之前所做的广泛诊断测试和分析。变化包括将每簇的孔数从 3 个减少到 1 个,并致力于极端有限的入口设计,穿孔可将入口孔水平推至 2,000 psi 的摩擦压力。

Hess 完井工程顾问 Ohm (Apiwat) Lorwongngam 表示,更长的阶段将每口井所需的数量减少了 12 个,并将完井成本降低了 10% 以上。

赫斯论文背后的有限进入思想在很多方面与德文郡论文是一致的。两者都支持极端的有限进入设计,并发现了每个阶段大量集群的问题。

Hess 论文中包含的图表显示,当簇数量接近 20 时,压裂均匀性显着降低,结果从那时开始恶化(图 1)。

随着簇数接近 22,治疗率和均匀性下降
图 1——Hess 的研究显示了当簇计数接近 22 时处理率和均匀性如何下降。
资料来源:SPE 212358。

Lorwongngam 表示,单孔簇数量的限制是基于每分钟可输送到每个孔的桶数,最少 4.5 桶左右。

“我们发现,我们可以将阶段中的总簇数增加到 20,同时保持较高的限制进入压力,并将每个簇的速率保持在 5.0 桶/分钟以上。我们已经测试了每口井多达 24 个簇,以了解上限,”他说。

Hess 目前的设计在位于侧向跟部附近的阶段最多有大约 18 个集群,在那里它可以提供处理所有这些孔所需的高流量。但靠近支管末端(趾部)的阶段有大约一半数量的集群,以补偿由于在通常 2 英里长的支管上遇到的摩擦而导致的较低泵率。

如果油价上涨并持续上涨,一次性设计还将使 Hess 能够通过添加更多单次井组以缩小间距来提高油井产量。

该报称,该设计将通过在不牺牲产量的情况下减少阶段数来节省资金。Lorwongngam 表示,根据该设计两年的使用情况,“每口井的产量超出了我们的内部预期”。

赫斯一直在寻找改进的方法。Lorwongngam 表示,Hess 目前正在使用光纤应变测量来测量裂缝扩展进行现场测试,并正在考虑如何评估其支撑剂是否得到有效分布。

现在考虑一下

随着时间的推移,工程师对变量的影响以及它们如何相互作用有了更好的认识。

克莱默说,“你可以玩很多不同的技巧”,通过调整从集群设计和射孔泵送的支撑剂到泵送速率和摩擦压力等变量。“你必须在所有这些事情上进行权衡。我想强调这一点。”

德文郡的压裂评估与常识不同的一个重要原因是操作员使用其开发的新方法收集了裂缝扩展的数据。

在 Eagle Ford 试验场,德文郡在距离重复压裂井 225 英尺的观测井中使用了光纤。应变测量显示了每个裂缝生长的位置。这些数据加上井内成像(测量压力泵送过程中入口孔的增长量)被用来测量裂缝效率。

他们观察到,22簇阶段产生的长裂缝数量最多,但这4条裂缝仅占观测井测量的长裂缝的18%左右。7簇阶段的表现优于它,平均有2.5条长裂缝,比率为35%。

当他们分析数据时,具有高射孔摩擦力的 7 簇级具有 100% 的簇效率。22 簇阶段最低,为 78%,12 簇阶段介于两者之间。

在簇数最高的阶段中,论文观察到所有主要骨折都从阶段的脚跟侧生长出来,这表明脚趾侧的骨折受到的刺激很差。

德文郡的论文称,“这一观察结果表明,高簇数设计对不太占主导地位的簇的刺激不足,证实了穿孔成像结果。”

克莱默根据沙子分布添加了一个关于较短阶段的违反直觉的论点。他的想法是,吸收最多液体的主要星团并不总是吸收那么多沙子。在这些情况下,随着时间的推移,支撑不良可能会削弱大裂缝的产量。

对于这种差异的一个词解释就是惯性。当泥浆到达第一个穿孔时,高流速将流体推入入口孔,而较少部分较重的砂粒进入那里。克莱默说,较重的沙粒的惯性意味着大部分沙粒最终会进入井趾端附近的入口孔,那里的流速较低。

这种听起来合乎逻辑的可能性已经被讨论了很多年,但没有足够现实的测试来说服工程师放弃流体和沙子流出量大致相等的假设,或者支持创建更现实的沙子分布公式。

克莱默也有疑虑,但当加拿大康菲石油公司的一位工程师担心处理压力高于预期时,他​​决定尝试改变集群设计,看看是否会降低压力,他的想法开始发生变化。

克莱默说,他希望通过在套管高侧连续打两到三个孔来平衡沙子分布,并解决这些较高压力读数的其他可能解释。结果令人鼓舞,井后诊断表明支撑剂分布要好得多,但没有论文提供具体细节。

每个簇添加更多孔是有成本的。较大的簇会增加每个阶段所需的液体量,以确保所有这些孔都受到刺激。通常,解决方案是减少簇的数量,从而缩短阶段。

去年,GEODynamics 在一篇论文中报道了迄今为止最接近实际的沙子流出测试,该论文使用了全尺寸的舞台模型,可以对水和沙子的流量进行表面测量(SPE 209178)。

GEODynamics 的高级工程技术顾问史蒂夫·鲍姆加特纳 (Steve Baumgartner) 表示,8 簇和 13 簇配置的测试结果与吸收最多水的簇总是吸收最多沙子的假设背道而驰。在表面测试中起关键作用。

“更多的 40/70 目沙子最终出现在脚趾侧的簇中,而不是出现在脚跟侧的簇中,”他说(图 2)。他们的测试表明,100 目的沙子中的较小颗粒并非如此,这些颗粒“与液体保持一致,并且能够在从跟部到趾部的所有簇中转弯。”

断裂面测试
图 2——GEODynamics 的压裂面测试表明,最后到达的簇(趾侧)吸收了最多的支撑剂(40/70 目)。
资料来源:SPE 209141。

他说,当他们测量测试后收集的液体和沙子时,他们发现 100 目沙子更有可能在所有簇中均匀地流出。

赛段处罚减少

随着该行业转向更长的阶段,这样做的成本/效益随着压裂阶段之间的过渡时间的缩短而缩小。

从一口井到下一口井来回切换的拉链式压裂允许对一口井进行泵送,同时电缆工作人员在第二口井上进行下一阶段的射孔,作为这种来回模式的一部分,第二口井正在压裂。

马约尔加表示,同步压裂允许同时进行多级压裂,这推动了对超大型泵的需求。

各阶段之间的平均时间已从十年前的 45 分钟缩短到现在的 25 分钟或更短,包括 SLB 在内的服务公司正在开发自动化泵送和电缆管理系统,以期进一步缩短时间。

改进的硬件和日益自动化的控制系统也减少了切换时间,但该行业距离 24/7 泵送的目标还很远。

SEF Energy 业务开发和技术副总裁 Tim Marvel 表示,如今的工作平均每天工作约 16 个小时。该公司持有的公司包括 Downing,该公司正在开发一种自动化完井系统,以减少阶段之间的时间,以达到 24/7 压裂的目标。

“我们每天都会进来查看基于时间的活动图表上显示的阶段之间的空白,看看我们可以消除多少,”他说。

Marvel 表示,他们的自动化系统目前允许用户平均每天泵送 20 小时。它通过减少阶段之间的过渡时间、允许在过渡期间连续泵送以及自动化电缆操作来实现这一点。该机器包括一个装置,可在每次使用后向阀门涂抹适量的润滑脂。

Marvel 的工作还需要找到一种方法来说服运营商付费使用自动化系统,并调整他们的运营以适应这种变化。在俄克拉荷马城研讨会上的演讲中,他建议缩短阶段的转变可能会提供一个机会。

“如果阶段之间没有时间损失,你们会选择较短的阶段吗?”漫威在研讨会上问道(SPE 213101)。

Lorwongngam 同意,如果他们能够每天近 24 小时抽水,井中的级数对总体成本的影响就会更小。但他表示,仍需要考虑每级钢丝绳运行和射孔枪的成本。

即使实现了所有这些自动化,每天仍然有平均 4 小时的停机时间,其中大部分时间都花在更换因泵送大量水和沙子而损坏的泵上。

Marvel 同意,维修停机时间仍然是一个主要成本项目,也是 24/7 运营的障碍。在他的演讲中,他报告了该公司机器人系统在井场的成功演示,该系统可以安全地移除损坏的泵并更换为新泵,而在压裂继续进行的过程中,无需在红色区域进行人工操作。

“自动泵更换使您可以在不停止垫操作的情况下进行维护,”Marvel 说。过去,他们已经展示了一两个泵的功能。

“大多数压裂泵上部署的第一批商业车队将在七月/八月的时间范围内部署,”他说。

根据他的计算,该系统可以将阶段之间的时间减少到 30 秒,增加每天的泵送时间,并使工人远离危险的地方。

“泵送速度稍微减慢;我们不会停止。我们转换拉链并重新启动,”漫威说,他说这种变化“几乎是瞬时的。”


更换泵

  • 泵被隔离,压力被降低,并且泵被脱开。
  • 泵车被移出进行维修或更换。
  • 另一辆泵车倒车至该位置。
  • 驱动臂将自动泵交换滑橇与安装在卡车后部的板连接起来,并将板夹紧在一起。
  • 连接经过压力测试,泵压力平衡,并向导弹打开并恢复在线状态。

资料来源:SPE 213101。

唐宁换泵系统
唐宁泵更换系统可以与任何泵配合使用,但需要通过板将高压和低压软管固定到位,以确保它们位于正确的位置以进行自动连接。
资料来源:唐宁。

供进一步阅读

SPE 212340 重新定义 Eagle Ford 的可采储量:从水力压裂试验场 1 (HFTS) 第 3 阶段中汲取的折射和填充开发经验教训,作者: Devon Energy 的 K. Brinkley、C. Thompson 和 J. Haffener 等。

SPE 212358 One Shot Wonder XLE Design:在巴肯开发 XLE 设计的持续改进案例研究, 作者:AO Lorwongngam、M. McKimmy 和 E. Oughton 等人,Hess Corp.

SPE 213101 自动完井地面系统:24/7 压裂之路, 作者:T. Marvel,SEF Energy;A.约翰逊,唐宁;P. Douget 和 Michael Mast,Blue Ox Resources 等。

SPE 209141 前两次地面测试的执行和经验教训,复制非常规压裂和支撑剂输送,作者: GEODynamics Inc. 的 P. Snider 和 S. Baumgartner;和 M. Mayerhofer,Liberty Oilfield Services 等。

SPE 209178 基于支撑剂传输表面测试对套管和射孔中的支撑剂传输进行建模 ,作者:Oil States Energy Services 的 J. Kolle;A. Mueller,ACMS LLC;和 S. Baumgartner,GEODynamics 等人。

原文链接/jpt
Unconventional/complex reservoirs

After Years of Ever-Longer Fracturing Stages, Some Engineers Say Shorter Can Be Better

The trend in fracturing designs has been longer stages with more perforation clusters, which save time and money. But there are a couple of companies testing whether shorter is better for production.

A fracturing site where two large white units from Downing house an automated system that controls the flow of slurry from the pumps into a well during fracturing.
A fracturing site where two large white units from Downing house an automated system that controls the flow of slurry from the pumps into a well during fracturing.
Source: Downing.

The trend in fracturing designs has been longer stages with more perforation clusters, which save time and money.

Based on papers at this year’s SPE Hydraulic Fracturing Technology Conference and Exhibition, the thinking that has sharply reduced the number of perforations per cluster and improved the effectiveness of fracturing is becoming the industry norm.

But there are a couple of companies questioning the consensus by fracturing wells with shorter stages and fewer clusters to see if they deliver more oil and gas production.

ConocoPhillips has been considering “going backward to fewer clusters per stage,” said Dave Cramer, a senior engineering fellow at the company.

“In some areas, we are testing out fewer clusters per stage based on fiber-based observations in offset wells that (indicate) far‑field treatment uniformity is improved as a result,” he said, adding “another advantage of reducing stage length is that injection rate into the hydraulic fractures is increased, which leads to increased fracture width and improved proppant transport.”

The offset-well observations mentioned were in a recent paper by Devon Energy that reported on a test which concluded that stages with fewer clusters were more efficiently fractured than longer stages with more of them (SPE 212340).

The 36-page paper was based on extensive testing at Phase 3 of the Hydraulic Fracturing Test Site 1 in the Eagle Ford, where a well fractured using a wide range of clusters per stage was used to find a way to most effectively refracture productive rock missed by an old fracture design.

The data were shared with companies backing the private-public partnership with the US Department of Energy, which included ConocoPhillips.

The paper’s authors wrote, “Generally, cluster efficiencies are higher for stage designs with fewer clusters.”

Cluster efficiency depends on the entry holes in a cluster getting enough fluid at a high enough rate to create a productive fracture. Fracture length is the result of other choices, including the pump rate, the entry-hole numbers, diameter, and placement.

The thinking behind these designs—as with most fracturing nowadays—is based on the limited‑entry method. This technique ensures the pumping rate and fluid volumes are enough to properly stimulate all the perforations, which are sized and placed to ensure all the entry holes have a chance of developing a fracture.

The industry’s focus on equalizing treatment goes back to early studies using fiber optics that revealed that the first clusters passed nearest the heel side of the lateral were taking in the lion’s share of the fluid and developing dominant fractures, leaving many later clusters under stimulated.

Based on recent papers from Devon and Hess, limited-entry ensures most clusters are stimulated, but dominant clusters are still getting more than their share because the high flow rates that favor them with more fluid also ensure they erode faster, allowing them to take in more fluid.

“Regardless of intended design, the stimulation is making a similarly sized dominant fracture and is taking a similar amount of fluid,” the Devon paper said. That means the fluid flow remaining for later stages is roughly similar, whether there are 10 more clusters to stimulate or 20 of them.

Based on Devon’s test well results, fracturing efficiency declined as the number of clusters per stage rose. Some loss of efficiency is an acceptable tradeoff, given the higher cost of fracturing more stages. But the data suggests there’s a limit.

“The total (pumping) rate is not enough to fracture all 22 perfs. That limits what you can get out of those toe clusters,” said Jackson Haffener, a geophysicist for Devon, when delivering a presentation about the paper at the SPE Oklahoma City Oil and Gas Symposium.

At the symposium, Haffener said that with new, shorter stage designs, “We are now leaving less resource behind with lower cluster counts.”

Cramer said the production gains from shorter stages with fewer clusters are expected to be “meaningful.”

“We are always trying to reduce costs,” but “we may need to pay a little more to make the most profit,” he added.

Why Do That?

Those encouraging words fail to answer the obvious question for a completion engineer thinking about trying shorter stages with fewer clusters: How much more can a shorter stage produce?

The quotes above suggest shorter stages can deliver more oil and gas. But based on what has been disclosed, there’s little public information on whether going shorter can add the production needed to justify the cost of fracturing more stages. And that has become critical as public companies expand their share of major share plays.

“If they spend more money, there is a big push to know why,” said Justin Mayorga, vice president, shale supply chain research at Rystad.

The areas where companies are willing to spend more are proven ways to increase production; for example, companies are pumping more sand—with averages in the Permian rising from 2,200 pounds per ft to 2,500, he said. He added that reflects the rebound in sand production, which has brought prices down to affordable levels.

Companies are also spending more for extremely high-horsepower pumps—which can more efficiently deliver the pumping rate needed to effectively fracture multiple wells—and phasing out diesel-powered pumps in favor of ones running on lower-cost natural gas, Mayorga said.

And they are spending more on rounds of diagnostic testing and analysis to figure out the most-productive options when engineering wells.

A good example of that is the process Hess used to prove the ideas that went into its current design standard, described in a paper where the title called its new cluster design a “one-shot wonder” (SPE 212358).

It was an eye grabbing headline for an SPE report on field testing which supported the value of one-shot clusters. But upon further consideration, Hess’s team worried that readers could associate that phrase with songs that are “one-hit wonders,” which are the opposite of its systematic long-term performance improvement program.

The paper described the extensive diagnostic testing and analysis done before Hess changed its Bakken fracturing methods. Changes included reducing the number of holes per cluster from three to one and a commitment to extreme limited‑entry design, with perforations that push the entry-hole level to a friction pressure of 2,000 psi.

Longer stages reduced the number needed per well by 12 and cut completion costs by more than 10%, said Ohm (Apiwat) Lorwongngam, a completions engineering advisor at Hess.

The limited-entry thinking behind Hess’s paper is consistent with the Devon paper on many points. Both endorsed extreme limited-entry designs and identified issues with high numbers of clusters per stage.

The Hess paper included a chart showing there was a significant loss in fracturing uniformity as the number of clusters neared 20, and the results deteriorated from there (Fig. 1).

treatment rate and uniformity drop as the cluster count approached 22
Fig. 1—The study by Hess showed how the treatment rate and uniformity drop as the cluster count approached 22.
Source: SPE 212358.

Lorwongngam said the limit on the number of one-hole clusters is based on the number of bbl/min that can be delivered to each hole, with 4.5 being about the minimum.

“We found that we can increase the total clusters in a stage up to 20 while keeping high limited-entry pressure and keep rate per cluster above 5.0 bbl/min. We have tested up to 24 clusters per well to understand the upper boundary,” he said.

Hess’s current design tops off at around 18 clusters for stages located near the heel of the lateral, where it can deliver the high flow rate needed to treat all those holes. But stages near the end (toe) of the laterals have about half as many clusters to compensate for the lower pump rate that results from the friction encountered on laterals that are typically 2 miles long.

The one-shot design will also allow Hess to increase well production by adding more single-shot clusters for closer spacing if oil prices go up and stay up.

The paper said the design would save money by reducing stage counts without sacrificing production. Based on 2 years of using the design, “Hess production numbers per wells have exceeded our internal expectations,” Lorwongngam said.

And Hess is continually looking for ways to improve. Lorwongngam said Hess is now doing field tests using fiber-optic strain measures to measure fracture growth and is considering how to evaluate whether its proppant is being effectively distributed.

Now Consider This

Over time, engineers are getting a better feel for the impact of variables and how they interact.

“There are a lot of different tricks you can play” by adjusting variables ranging from the cluster design and the proppant pumped per perforation to the pumping rate and friction pressure, Cramer said. “You have got tradeoffs on all this stuff. I want to emphasize that point.”

A big reason Devon’s fracturing evaluations diverge from the common wisdom is the operator gathered data on fracture growth using a new method it developed.

At the Eagle Ford test site, Devon used fiber optics in an observation well 225 ft from a well that was being refractured. The strain measurement showed where each fracture grew. That data plus in-well imaging, which measured how much entry holes grew during pressure pumping, was used to measure fracture efficiency.

They observed that the 22-cluster stage produced the largest number of long fractures, but those four fractures represented only about 18% of the long fractures measured by the observation well. The 7-cluster stage outperformed it with an average of 2.5 long fractures—a 35% rate.

When they analyzed the data, the 7-cluster stages with high perforation friction had 100% cluster efficiency. The 22-cluster stages were the lowest, at 78%, with the 12-cluster stages in between.

In the stages with the highest cluster counts, the paper observed that all the dominant fractures grew out of the heel side of the stage, suggesting those on the toe side were poorly stimulated.

“The implication from this observation is high cluster count designs are understimulating the less-dominant clusters, corroborating the perforation imaging results,” the Devon paper said.

Cramer added a counterintuitive argument for shorter stages based on sand distribution. His thinking is that the dominant clusters that take in the most fluid do not always take in as much sand. In those cases, production from the big fracture is likely to be undercut by poor propping over time.

The one-word explanation for the disparity is inertia. The high flow rate as slurry reaches the first perforations pushes fluid into the entry hole while a lesser share of the heavier sand grains goes in there. The inertia of the heavier sand particles means much of it ends up in entry holes near the toe end of the well where the flow rate is lower, Cramer said.

That logical-sounding possibility has been talked about for years, but there was no test that was sufficiently realistic to convince engineers to drop their assumption that fluid and sand outflow is roughly equal, or to support the creation of more realistic sand distribution formulas.

Cramer had his doubts as well, but his thinking began to change when an engineer at ConocoPhillips in Canada who was concerned with higher-than-expected treating pressure decided to try changing the cluster design to see if that reduced it.

He was hoping to balance the sand distribution by going from two to three holes in a row on the high side of the casing and address other possible explanations for those higher pressure readings, Cramer said. The results were promising, and the post-well diagnostics indicated much better proppant distribution, but there’s been no paper offering specifics.

There is a cost to adding more holes per cluster. Bigger clusters increase the amount of fluid needed per stage to ensure that all those holes are stimulated. Typically the solution is to reduce the number of clusters, resulting in a shorter stage.

The closest anyone has ever come to a realistic test of sand outflows was reported in a paper by GEODynamics last year using a full-sized stage model that allowed surface measurements of the flow of the water and sand (SPE 209178).

Its results from tests with 8- and 13-cluster configurations ran counter to the assumption that the cluster taking in the most water would always be taking in the largest amount of sand, said Steve Baumgartner, senior engineering technical advisor at GEODynamics, who played a key role in the surface test.

“More 40/70-mesh sand ends up in the toe-side clusters than in the heel-side clusters,” he said (Fig. 2). Their testing showed that is not the case with the smaller particles in 100-mesh sand which “stay with the fluid and are able to turn the corner in all clusters from heel to toe side.”

A fracturing surface test
Fig. 2—A fracturing surface test by GEODynamics showed that the last clusters reached (toe side) took in the most proppant (40/70-mesh).
Source: SPE 209141.

When they measured the fluid and sand collected after testing, they found 100-mesh sand was more likely to go out uniformly in all the clusters, he said.

Stage Penalty Shrinks

As the industry has shifted to longer stages, the cost/benefit of doing so has shrunk as the transition time between stages while fracturing goes down.

Zipper fracs that switch back and forth from one well to the next have allowed one well to be pumped while a wireline crew perforates the next stage on the second well that is being fractured as part of that back-and-forth pattern.

Simul-fracs allow multiple stages to be fractured at once, which is driving demand for extremely large pumps, Mayorga said.

The average time between stages has dropped from 45 minutes a decade ago to 25 minutes or less now, and service companies, including SLB, are developing automated pumping and wireline management systems that promise further reductions.

Improved hardware and increasingly automated control systems have also reduced switching times, but the industry is far from the goal of pumping 24/7.

The average job today is pumping approximately 16 hours a day, according to Tim Marvel, vice president for business development and technology at SEF Energy. The company’s holdings include Downing, which is developing an automated completion system, reducing the time between stages with the goal of fracturing 24/7.

“Every day we come in and look at the white space between stages as shown on a time-based activity chart and see how much we can eliminate,” he said.

Marvel said their automation system currently allows users to pump an average of 20 hours per day. It does that with features that reduce the transition time between stages, allow continuous pumping during transitions, and automate wireline operations. The machinery includes a unit that applies just the right amount of grease to valves after each use.

Marvel’s job also requires finding a way to convince operators to pay up to use an automated system and adapt their operations for that change. During a presentation at the OKC Symposium, he suggested a shift to shorter stages could offer an opening.

“If there is no time penalty between stages, would you go to shorter stages?” Marvel asked at the symposium (SPE 213101).

If they were able to pump nearly 24 hours a day, Lorwongngam agreed that the number of stages in the well would have less effect on the overall cost. But he said the cost of wireline runs and perforation guns per stage would still need to be considered.

Even with all that automation, there’s still an average of 4 hours a day of downtime, much of which is spent replacing pumps battered by pumping all that water and sand.

Marvel agrees that downtime for repairs remains a major cost item and a barrier to 24/7 operations. In his presentation, he reported on successful wellsite demonstrations of the company’s robotic system that can safely remove a broken pump and replace it with a new one with no humans required in the red zone while fracturing continues.

“Automated pump swapping allows you to do maintenance without stopping pad operations,” Marvel said. In the past they have demonstrated what they can do on a pump or two.

“The first commercial fleet to be deployed on the majority of the frac pumps will be deployed in July/August time frame,” he said.

By his accounting, the system can reduce the time between stages to 30 seconds, adding hours of pumping time per day and keeping workers out of dangerous places.

“The pumping slows a bit; we do not stop. We transition the zipper and start back up,” said Marvel, who said the change is “nearly instantaneous.”


To Change Out a Pump

  • The pump is isolated, the pressure is bled down, and the pump is uncoupled.
  • The pump truck is moved out for repairs or replacement.
  • Another pump truck is backed into that position.
  • Actuated arms couple the automated pump-swapping skid with a plate mounted to the back of the truck, and the plates are clamped together.
  • The connection is pressure tested, the pump is pressure equalized, and opened to the missile and brought back online.

Source: SPE 213101.

Downing pump-changing system
The Downing pump-changing system can work with any pump but requires the high- and low-pressure hoses to be fixed in place by a plate to ensure they are in the right spot for automated connections.
Source: Downing.

For Further Reading

SPE 212340 Redefining Recoverable Reserves in the Eagle Ford: Refracs and Infill Development Lessons Learned From the Hydraulic Fracturing Test Site 1 (HFTS) Phase 3 by K. Brinkley, C. Thompson, and J. Haffener, Devon Energy, et al.

SPE 212358 One Shot Wonder XLE Design: A Continuous Improvement Case Study of Developing XLE Design in the Bakken by A.O. Lorwongngam, M. McKimmy, and E. Oughton, et al., Hess Corp.

SPE 213101 Automated Completion Surface System: The Path to Fracturing 24/7 by T. Marvel, SEF Energy; A. Johnson, Downing; P. Douget and Michael Mast, Blue Ox Resources, et al.

SPE 209141 Execution and Learnings From the First Two Surface Tests Replicating Unconventional Fracturing and Proppant Transport by P. Snider and S. Baumgartner, GEODynamics Inc.; and M. Mayerhofer, Liberty Oilfield Services, et al.

SPE 209178 Modeling Proppant Transport in Casing and Perforations Based on Proppant Transport Surface Tests by J. Kolle, Oil States Energy Services; A. Mueller, ACMS LLC; and S. Baumgartner, GEODynamics, et al.