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Thermodynamic analysis of in-situ hydrogen from hot compressed water for heavy oil upgrading

机译:用于压缩重油的热压缩水中原位氢的热力学分析

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Due to many benefits of heavy oil upgrading in the green medium of hot compressed water (HCW), the present study considers the thermodynamic analysis of in-situ hydrogen created by partial oxidation of light hydrocarbons (HC) in HCW. The aim is seeking the upgrading condition where light hydrocarbons create hydrogen (H-2) and carbon monoxide (CO) assisted by partial oxidation of light hydrocarbons. The formed CO collaborates in insitu active hydrogen through water gas shift reaction (CO+H2O <-> H-2+CO2) which is more effective than external hydrogen for hydrogenation of heavy oil in HCW. Applying the powerful capability of Aspen Plus (R), i.e., sensitivity analysis, the effect of significant parameters, such as temperature, pressure (water density), water to oil ratio, and oxygen (O-2) to oil ratio are studied comprehensively in order to maximize the amount of active hydrogen. The results indicate that higher temperatures and the amount of water (H2O/heavy oil) are two favorable factors to increase the contribution of active hydrogen, while the pressure is not a determinant factor at supercritical condition (P >= 25 MPa). The formation of methane is also decreased at high temperature which is desired for upgrading system. The higher amount of water implies more quantity of O-2 since partial oxidation affords the enthalpy of auto-thermal reforming of HO. Hence there should be a compromise in the selected ratios of H2O/HC and O-2/HC in HCW upgrading system. A set of experiments are conducted in order to compare the simulation and experimental results. Although the experimental results are established on kinetic data which also reflect the physical effect of HCW during HO upgrading, however, the thermodynamic study provides valued information, in agreement with experiments, that improves our understanding of HO upgrading in HCW with less coke. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:由于在热压缩水(HCW)的绿色介质中重油提质的许多好处,本研究考虑了由HCW中轻烃(HC)的部分氧化产生的原位氢的热力学分析。目的是寻求一种升级条件,在这种条件下,轻烃会通过轻烃的部分氧化而产生氢(H-2)和一氧化碳(CO)。所形成的CO通过水煤气变换反应(CO + H 2 O-H-2 + CO 2)在原位与活泼氢协同作用,这比外部氢对HCW中重油的氢化更有效。利用Aspen Plus(R)的强大功能(即灵敏度分析),全面研究温度,压力(水密度),水油比和氧气(O-2)油比等重要参数的影响为了使活性氢的量最大化。结果表明,较高的温度和水量(H2O /重油)是增加活性氢贡献的两个有利因素,而压力在超临界条件下(P> = 25 MPa)不是决定因素。甲烷的形成在高温下也减少了,这是升级系统所需要的。由于部分氧化提供了HO自热重整的焓,因此较高的水含量意味着O-2的数量也更多。因此,在HCW升级系统中,H2O / HC和O-2 / HC的选定比例应有所妥协。为了比较仿真结果和实验结果,进行了一组实验。尽管实验结果是建立在动力学数据上的,该数据也反映了HCW在HO升级过程中的物理作用,但是,热力学研究与实验相一致,提供了有价值的信息,可增进我们对焦炭较少的HCW HO升级的理解。 (C)2019氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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