Dataset for the dimethyl sulfoxide as a novel thermodynamic inhibitor of carbon dioxide hydrate formation

Anton P Semenov; Rais I Mendgaziev; Andrey S Stoporev; Vladimir A Istomin; Daria V Sergeeva; Timur B Tulegenov; Vladimir A Vinokurov

doi:10.1016/j.dib.2022.108289

Dataset for the dimethyl sulfoxide as a novel thermodynamic inhibitor of carbon dioxide hydrate formation

Data Brief. 2022 May 17:42:108289. doi: 10.1016/j.dib.2022.108289. eCollection 2022 Jun.

Authors

Anton P Semenov¹, Rais I Mendgaziev¹, Andrey S Stoporev^{1

2}, Vladimir A Istomin^{1

3}, Daria V Sergeeva^{1

3}, Timur B Tulegenov¹, Vladimir A Vinokurov¹

Affiliations

¹ Gubkin University, Department of Physical and Colloid Chemistry, 65, Leninsky prospekt, Building 1, 119991, Moscow, Russian Federation.
² Nikolaev Institute of Inorganic Chemistry SB RAS, Ac. Lavrentiev ave. 3, 630090, Novosibirsk, Russian Federation.
³ Skolkovo Institute of Science and Technology (Skoltech), Nobelya Str. 3, 121205, Moscow, Russian Federation.

Abstract

The temperatures and pressures of the three-phase equilibrium V-L_w-H (gas - aqueous solution - gas hydrate) were measured in the CO₂ - H₂O - dimethyl sulfoxide (DMSO) system at concentrations of organic solute in the aqueous phase up to 50 mass%. Measurements of CO₂ hydrate equilibrium conditions were carried out using a constant volume autoclave by continuous heating at a rate of 0.1 K/h with simultaneous stirring of fluids by a four-blade agitator at 600 rpm. The equilibrium temperature and pressure of CO₂ hydrate were determined for the endpoint of the hydrate dissociation in each experiment. The CO₂ gas fugacity was calculated by the equation of state for carbon dioxide for the measured points. The flow regime in the autoclave during the operation of the stirring system was characterized by calculating the Reynolds number using literature data on the viscosity and density of water and DMSO aqueous solutions. We employed regression analysis to approximate the dependences of equilibrium pressure (CO₂ gas fugacity) on temperature by two- and three-parameter equations. For each measured point, the value of CO₂ hydrate equilibrium temperature suppression ΔT_h was computed. The dependences of this quantity on CO₂ gas fugacity are considered for all DMSO concentrations. The coefficients of empirical correlation describing ΔT_h as a function of the DMSO mass fraction in solution and the equilibrium gas pressure are determined. This article is a co-submission with a paper [1].

Keywords: Carbon dioxide; Dimethyl sulfoxide; Gas hydrate inhibitor; Gas hydrates; Phase equilibria.