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Performance Analysis of Texas Eagle Ford Shale Oil Hydro Fracturing Produced Water Treatment Process

机译:德克萨斯鹰福特石油油水压裂生产水处理过程的性能分析

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With the rise of horizontal drilling, hydraulic fracturing has become increasingly common and it is estimated that 90 percent of new wells drilled in the United States are hydraulically fractured. Hydraulic fracturing involves the injection of a very large quantity of high pressure liquid to fracture the rock formation and pry open the fracture. This fracturing allows natural gas/oil to flow freely from the formation into the well for collection. The components used in the hydraulic fracturing process consist primarily of water, sand, salts, gel, diluted acid, surfactant corrosion inhibitor, scale inhibitor, and other additives to aid in the hydro fracturing process. During the hydro fracturing operation when the pressure used to inject the fracturing fluid into the well is released, some of the fluid returns to the surface; this fluid is called 'flowback' water. Once gas production begins at the well, all wastewater emerging from the well is called 'produced water'. Both types of wastewater – flowback and production phase water – contain potentially harmful constituents. These constituents can be broadly grouped into several principle categories: salts, organic hydrocarbons, metals, chemical additives and some naturally occurring radioactive material. Because of these constituents, shale oil/gas wastewater should not be released into the environment without adequate treatment. The purpose of this paper is to report the performance analysis of a water treatment process of Texas Eagle Ford Shale oil hydro fracturing produced. The treatment process consists of four primary unit operations: Adsorption column, Reverse osmosis, Ion-Exchange and Pump. The produced water is first pumped through the adsorption column, then a second high-pressure pump which then forces the water through the reverse osmosis membrane. The permeate of the membrane then flows through two ion exchange columns and received in a collection bin. Adsorption is the adhesion of atoms, ions, or molecules from a fluid or dissolved solid to an insoluble surface and is used to remove suspended organics like oil and grease as well as dissolved organics like benzene and toluene. Our adsorption column consists of a cartridge and housing unit rated for operating pressures of 90 psi and temperatures no higher than 125 °F. The cartridge was 10' tall and accepted 10' x 4.5' cartridges. Reverse osmosis filters work on the principle of membrane divergence. An extremely high pressure (800 psi in our process) is applied at the housing entrance that forces the fluid through the fine membrane. Due to the pressure spike, particles that are small enough pass through the fine holes in the filter transfer, while the larger particles are rejected and thus removed from the membrane. In our application, the reverse osmosis membrane rejected the ions and other larger particles like metals, minerals, and organics, allowing only water and smaller particles to remain. The membrane we used is a FilmTec Sea Water Membrane designed to handle increased salinity (greater than 10,000 ppm). The reverse osmosis unit operation used had a flow ratio of permeate to retetante of 73 to 27, which was determined by a series of mass balances across the unit operation. We used a mixed ion exchange in order to remove any remaining positive or negative ions. Our process consists of two ion exchange columns in parallel, both of which were 20' vertical columns housed in separate units. The process uses two pumps. The first pump transferred the water from the tank to the adsorption column at a low pressure. The second pump primed the system to the operating pressure, 800 psi, to transfer the produced water through the reverse osmosis membrane and the ion exchange. Each water sample analyzed was obtained from one of 4 major positions. Position 1: the untreated water, Position 2: after the activated carbon operation, Position 3: after the reverse osmosis operation and Position 4: after the ion exchange operation.
机译:随着水平钻孔的升高,水力压裂变得越来越普遍,据估计,美国在美国钻出的90%的新井是液压破裂。液压压裂涉及注入大量高压液体以裂缝岩层和撬开骨折。这种压裂允许天然气/油从地层自由流入井收集。液压压裂过程中使用的组件主要由水,砂,盐,凝胶,稀释的酸,表面活性剂腐蚀抑制剂,抑制剂和其他添加剂提供帮助,以帮助氢气压裂过程。在水电压裂操作期间,当用于将压裂流体注入井中的压力被释放时,一些流体返回到表面;这种流体称为“回流”水。一旦气体生产始于井,所有从井中出现的废水都被称为“生产的水”。两种类型的废水 - 流量和生产相水 - 含有潜在有害的成分。这些成分可以广泛地分组为几个原则类别:盐,有机烃,金属,化学添加剂和一些天然存在的放射性物质。由于这些成分,不应释放出来的物质油/气废水而不适当处理。本文的目的是报告生产的德克萨斯鹰福特流油水力压裂水处理过程的性能分析。处理过程由四个主要单元操作组成:吸附柱,反渗透,离子交换和泵。首先将产生的水通过吸附柱泵送,然后是第二高压泵,然后第二高压泵迫使水通过反渗透膜。然后膜的渗透物流过两个离子交换柱并在收集箱中接收。吸附是原子,离子或分子来自流体或溶解的固体与不溶性表面的粘附性,并且用于除去悬浮的有机物,如油和润滑脂,以及苯和甲苯等溶解的有机物。我们的吸附柱包括墨盒和外壳单元,用于操作压力为90psi,温度不高于125°F。墨盒是10英尺高的,接受10'x 4.5'墨盒。反渗透过滤器对膜分歧原理工作。极高的压力(我们的过程中800psi)施加在燃烧通过细膜的壳体入口处。由于压力尖峰,足够小的颗粒通过过滤器转移中的细孔,而较大的颗粒被拒绝并从膜中除去。在我们的应用中,反渗透膜拒绝了金属,矿物和有机物等离子和其他较大的颗粒,允许仅留下水和较小的颗粒。我们使用的膜是Filmtec海水膜,旨在处理增加的盐度(大于10,000ppm)。所用的反渗透单元操作具有渗透物的流动比率为73至27,其通过整个单元操作的一系列质量余量确定。我们使用了混合离子交换,以除去任何剩余的正或负离子。我们的进程由两个并联的离子交换柱组成,两者都是20'垂直柱,位于单独的单元中。该过程使用两个泵。第一泵以低压将水从罐中的水转移到吸附柱。第二泵将系统喷射到操作压力,800psi,通过反渗透膜和离子交换将产生的水转移。分析的每个水样品是从4个主要位置中的一种获得的。位置1:未处理的水,位置2:在活性炭操作后,位置3:在反渗透运行和位置4之后:离子交换操作后。

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