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关于寻找酒精与盐之间协同作用以生产更高效且环境友好型气体水合物抑制剂的数据。

Data on searching for synergy between alcohol and salt to produce more potent and environmentally benign gas hydrate inhibitors.

作者信息

Semenov Anton P, Mendgaziev Rais I, Istomin Vladimir A, Sergeeva Daria V, Vinokurov Vladimir A, Gong Yinghua, Li Tianduo, Stoporev Andrey S

机构信息

Gubkin University, Department of Physical and Colloid Chemistry, 65, Leninsky prospekt, Building 1, 119991 Moscow, Russian Federation.

Skolkovo Institute of Science and Technology (Skoltech), Nobelya Str. 3, 121205 Moscow, Russian Federation.

出版信息

Data Brief. 2024 Feb 9;53:110138. doi: 10.1016/j.dib.2024.110138. eCollection 2024 Apr.

Abstract

In order to systematically study the synergistic effect of gas hydrate inhibition with mixtures of methanol (MeOH) and magnesium chloride (MgCl), the impact of these compounds on the thermodynamic stability of methane hydrate in the systems of CH-MeOH-HO, CH-MgCl-HO, and CH-MeOH-MgCl-HO was experimentally investigated. The pressure and temperature conditions of the three-phase vapor-aqueous solution-gas hydrate equilibrium were determined for these systems. The resulting dataset has 164 equilibrium points within the range of 234-289 K and 3-13 MPa. All equilibrium points were measured as the endpoint of methane hydrate dissociation during the heating stage. The phase boundaries of methane hydrate were identified for 8 systems with MeOH (up to 60 mass%), 5 MgCl solutions (up to 26.7 mass%), and 14 mixtures of both inhibitors. Most equilibrium points were measured using a ramp heating technique (0.1 K/h) under isochoric conditions when the fluids were stirred at 600 rpm. It was found that even a 0.5 K/h heating rate for the CH-MgCl-HO system at low salt concentrations, along with all mixed aqueous solutions with methanol, gives results that do not differ from 0.1 K/h, considering the measurement uncertainties. Most measurements for the CH-MgCl-HO system at high salt content were acquired using a step heating technique. The coefficients of the empirical equations approximating the equilibrium points for each inhibitor concentration were defined. The change in the slope parameter of the empirical equation was analyzed as a function of inhibitor content. Correlations that accurately describe the thermodynamic inhibition effect of methane hydrate with methanol and magnesium chloride on a mass% and mol% scale were obtained. The freezing temperatures of single and mixed aqueous solutions of methanol and magnesium chloride were determined experimentally to confirm the thermodynamic consistency of the methane hydrate equilibrium data.

摘要

为了系统地研究甲醇(MeOH)和氯化镁(MgCl)混合物对气体水合物抑制的协同作用,通过实验研究了这些化合物对CH - MeOH - HO、CH - MgCl - HO和CH - MeOH - MgCl - HO体系中甲烷水合物热力学稳定性的影响。测定了这些体系的气 - 水溶液 - 气体水合物三相平衡的压力和温度条件。所得数据集在234 - 289 K和3 - 13 MPa范围内有164个平衡点。所有平衡点均在加热阶段作为甲烷水合物解离的终点进行测量。确定了8种含甲醇体系(质量分数高达60%)、5种MgCl溶液(质量分数高达26.7%)以及14种两种抑制剂混合物体系的甲烷水合物相边界。大多数平衡点是在等容条件下,流体以600 rpm搅拌时,采用斜坡加热技术(0.1 K/h)测量得到的。研究发现,对于低盐浓度的CH - MgCl - HO体系,即使加热速率为0.5 K/h,以及所有含甲醇的混合水溶液,考虑到测量不确定度,其结果与0.1 K/h并无差异。对于高盐含量的CH - MgCl - HO体系,大多数测量是采用阶梯加热技术进行的。定义了近似每种抑制剂浓度平衡点的经验方程系数。分析了经验方程斜率参数随抑制剂含量的变化。获得了能准确描述甲烷水合物在质量分数和摩尔分数尺度上与甲醇和氯化镁的热力学抑制作用的相关性。通过实验测定了甲醇和氯化镁单一及混合水溶液的冰点,以确认甲烷水合物平衡数据的热力学一致性。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/6d4e/10877679/8ef9ec4e67b3/gr1.jpg

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