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Treatment of Aqueous waste streams contaminated with carbon dioxide and crude oil from an enhanced oil recovery process, Mahmood Alimahmoodi.

机译:Mahmood Alimahmoodi通过强化采油工艺处理被二氧化碳和原油污染的含水废水。

摘要

In the process of Enhanced Oil Recovery (EOR), carbon dioxide and water are used excessively (8000 ft 3 of CO 2 and 10 bbl of water per 1 bbl oil extracted) to increase the oil production and as a result, a large stream of waste water is generated. The main contaminants of this waste are dissolved gases mainly CO 2 and dissolved petroleum hydrocarbons (referred to as TPH). CO 2 which forms about 70% of the greenhouse gases. is the major cause of global warming and its atmospheric concentration (currently 385 ppm) has been rapidly increasing since the past decades. In a series of batch experiments, the application of several electron donors such as simple volatile fatty acids and mono and disaccharides were investigated to remove CO 2 and TPH from a synthetic waste stream (containing about 200 mg COD/L of TPH and dissolved CO 2 at the saturation level). About 95% of CO 2 and 76% of TPH were removed using formate (2 g/L) and sucrose (2.5 g/L) respectively at a mesophilic range of temperature (about 35°C). In the second phase of this study, a two-step reactor system was used to treat this waste and the system operation was optimized using the method of evolutionary operation (EVOP) factorial design. For the first reactor with CO 2 reduction and CH 4 production as the target parameters, values of pH, temperature and organic loading rate of 2.5, 38°C and 6240 mg COD/L were obtained. The corresponding values for the second reactor were 6.5, 39.5°C and 394 mg COD/L for the TPH removal. The energy balance for the system resulted in the calculated net energy ratio (NER) of 3.7 which showed a sustainable biogas production. The kinetic study of the system showed that degradation of formate and sucrose in both reactors is affected by the presence of petroleum hydrocarbons probably due to their inhibitory effects. Also, it was shown that the original differential equations for the substrate concentration and microbial growth can better predict the kinetic behavior of the system than the simplified models. As the overall conclusion of this study, this method is less complex compared to other competitive methods and it can be easily applied. Moreover, besides its low energy requirements, it can generate CH 4 from CO 2 as a clean source of energy.
机译:在提高采油率(EOR)的过程中,过量使用了二氧化碳和水(每提取1桶石油,要消耗8000 ft 3的CO 2和10桶水),从而增加了石油的产量,因此,产生废水。该废物的主要污染物是溶解气体,主要是CO 2和溶解的石油碳氢化合物(称为TPH)。 CO 2占温室气体的70%。是全球变暖的主要原因,并且自过去几十年来,其大气浓度(目前为385 ppm)一直在迅速增加。在一系列的分批实验中,研究了几种电子给体(如简单的挥发性脂肪酸以及单糖和双糖)的应用,以从合成废物流(含约200 mg COD / L的TPH和溶解的CO 2中)去除CO 2和TPH。在饱和水平)。在中温温度范围(约35°C)下,分别使用甲酸盐(2 g / L)和蔗糖(2.5 g / L)除去约95%的CO 2和76%的TPH。在这项研究的第二阶段,使用了两步反应器系统来处理该废物,并使用进化操作(EVOP)因子设计方法优化了系统操作。对于以CO 2还原和CH 4产生为目标参数的第一个反应器,获得的pH值,温度和有机负载率为2.5、38°C和6240 mg COD / L。 TPH去除的第二个反应器的相应值为6.5、39.5°C和394 mg COD / L。系统的能量平衡导致计算出的净能量比(NER)为3.7,表明可持续的沼气生产。该系统的动力学研究表明,两个反应器中甲酸酯和蔗糖的降解都可能受到石油烃的存在的影响,这可能是由于它们的抑制作用所致。此外,结果表明,与简化模型相比,原始的底物浓度和微生物生长微分方程可以更好地预测系统的动力学行为。作为本研究的总体结论,与其他竞争方法相比,该方法更为简单,并且可以轻松应用。此外,除了能耗低之外,它还可以从CO 2生成CH 4作为清洁能源。

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    Alimahmoodi Mahmood;

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  • 年度 2009
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