Effect of heating rate on the accuracy of measuring equilibrium conditions for methane and argon hydrates

被引:35
作者
Semenov, Anton Pavlovich [1 ]
Medvedev, Vladimir Igorevich [1 ]
Gushchin, Pavel Aleksandrovich [1 ]
Yakushev, Vladimir Stanislavovich [2 ]
机构
[1] Gubkin Russian State Univ Oil & Gas, Dept Phys & Colloid Chem, Moscow 119991, Russia
[2] Gubkin Russian State Univ Oil & Gas, Fed State Budgetary Educ Inst Higher Vocat Educ, Gas Prod Dept, Moscow 119991, Russia
关键词
Gas hydrates; Methane hydrate; Argon hydrate; Isochoric method; Heating rate; Sodium dodecyl sulfate; DISSOCIATION;
D O I
10.1016/j.ces.2015.06.031
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work examined the effect of the heating rate (from 0.2 K/h (5.56 . 10(-5) K/s) to 10 K/h (277.78 . 10-5 K/s)) on the accuracy of measuring the three-phase equilibrium conditions for gas-liquid water-hydrate systems. The H(2)On+CH4 (CS-I) system was studied over the temperature range of 274.2-285.2 K and the pressure range of 3.0-9.0 MPa. Additionally, the H2O+Ar (CS-II) system was studied over the temperature and pressure ranges of 273.7-280.2 K and 9.5-18.5 MPa, respectively. The hydrate formation/dissociation experiments were performed in a Sapphire Rocking Cell RCS6 under isochoric conditions. Gas hydrates were formed using a 0.1% (w/w) solution of sodium dodecyl sulfate. It was found that the dissociation of the methane and argon hydrates (CS-I and CS-II, respectively) proceeds under conditions close to equilibrium at heating rates up to 0.5 K/h (13.89. 10-5 K/s). Significant deviations of the P,T-curve from the equilibrium line are observed at higher heating rates for methane hydrate ( > 281.2 K) and argon hydrate ( > 2772 K). Our data on the equilibrium conditions of argon hydrate complement previous published data over the temperature range of 273.7-2802 K and the pressure range of 9.5-18.5 MPa. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:161 / 169
页数:9
相关论文
共 26 条
[1]   HYDRATES OF CARBON-DIOXIDE AND METHANE MIXTURES [J].
ADISASMITO, S ;
FRANK, RJ ;
SLOAN, ED .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1991, 36 (01) :68-71
[2]  
BENEDICT M, 1951, CHEM ENG PROG, V47, P419
[3]  
Burgass, 2002, P 4 INT C GAS HYDR Y, P380
[4]   OCCURRENCE OF METHANE HYDRATE IN SATURATED AND UNSATURATED SOLUTIONS OF SODIUM-CHLORIDE AND WATER IN DEPENDENCE OF TEMPERATURE AND PRESSURE [J].
DEROO, JL ;
PETERS, CJ ;
LICHTENTHALER, RN ;
DIEPEN, GAM .
AICHE JOURNAL, 1983, 29 (04) :651-657
[5]  
Dyadin YA, 1997, MENDELEEV COMMUN, P32
[6]   Experimental determination of methane hydrate dissociation curve up to 55 MPa by using a small amount of surfactant as hydrate promoter [J].
Gayet, P ;
Dicharry, C ;
Marion, G ;
Graciaa, A ;
Lachaise, J ;
Nesterov, A .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (21) :5751-5758
[7]  
Istomin V. A., 1992, GAS HYDRATES NATURAL
[8]   Experimental determination and modeling of structure II hydrates in mixtures of methane plus water plus 1,4-dioxane [J].
Jager, MD ;
de Deugd, RM ;
Peters, CJ ;
Arons, JD ;
Sloan, ED .
FLUID PHASE EQUILIBRIA, 1999, 165 (02) :209-223
[9]   Hydrate-containing phase equilibria for mixed guests of carbon dioxide and nitrogen [J].
Kim, Sun Hyung ;
Do Seo, Myoung ;
Kang, Jeong Won ;
Lee, Chul Soo .
FLUID PHASE EQUILIBRIA, 2011, 306 (02) :229-233
[10]  
Kutergin, 1992, INFLUENCE SURFACTANT, V323, P549