NOTE Pressure and Temperature Conditions for in Sodium Chloride
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Geochemical Journal, Vol. 29, pp. 325 to 329, 1995 NOTE Pressure and temperature conditions for methane hydrate dissociation in sodium chloride solutions TATSUO MAEKAWA, SHIRO ITOH*, SUSUMU SAKATA, SHUN-ICHIROIGARI and NOBORU IMAI Geological Survey of Japan, 1-1-3, Higashi, Tsukuba, Ibaraki 305, Japan (Received April 3, 1995; Accepted August 4, 1995) The pressure and temperature conditions were experimentally determined for methane hydrate disso ciation in sodium chloride solutions, and an empirical equation of the conditions was obtained in the pressure range up to 18 MPa. The present results indicate that the maximum depth of oceanic sediments where methane hydrate is stable increases as water depth to seafloor increases, and that the maximum depth in saline water is smaller than that in pure water. The difference in the depth between saline and pure waters increases with decreasing the water depth, indicating that salinity of pore water affects sig nificantly the amount of methane hydrate in oceanic sediments, in particular, beneath seafloor at relatively shallow depths. globally widespread and contain a large amount INTRODUCTION of methane in the crystalline structure, methane Methane hydrate is ice-like solid which is hydrates are expected to be a potential energy re composed of methane and water, and a kind of source in the near future. clathrates in which methane molecules are trapped Most of methane hydrates are suggested to in a cage-like crystal lattice of water molecules. occur in oceanic sediments in outer continental Methane hydrate contains a large amount of margins. The methane hydrates form from the methane gas; 1 m3 of methane hydrate can contain mixture of naturally occurring methane and pore up to 164 m3 of methane gas at standard tem water whose salinity is similar to seawater; about perature and pressure (Kvenvolden, 1993). Meth 3.5%. It has been known that the stability of ane hydrates are stable in conditions where high methane hydrate in saline water decreases as the pressure, low temperature and abundant supply of salinity of water increases. It is therefore important methane are present, and naturally occur in stable to investigate the stability of methane hydrate in form in the permafrost and sediments beneath saline water for estimating the amount of methane seafloor. The total amount of methane trapped in hydrate in oceanic sediments. methane hydrates in the world is estimated to be The conditions for methane hydrate dissocia 2 x 1016m3 (1 x 1019 g of methane carbon). Since tion in saline water up to 13 MPa has been deter the amount of carbon in methane hydrates is twice mined by several studies (Kobayashi et al., 1951; as large as the amount of organic carbon in fossil de Roo et al., 1983). However, natural methane fuel deposits known until now, methane hydrate hydrates often occur at depths deeper than 1300 could be a major reservoir of carbon in the crust m, equivalent to hydrostatic pressure of 13 MPa. (Kvenvolden, 1988). Because methane hydrates are Therefore, it is necessary to know the stability *Present address: Geoscience Laboratory , Geological Survey of Pakistan, Chak Shahzad P.O. Box 1461, Islamabad, Pakistan 325 326 T. Maekawa et al. conditions of methane hydrates in a higher pres light beam from the lamp is introduced into the sure range. In this study, we have determined the solution through the window from one side of the stability of methane hydrate at pressures up to 18 hydrate cell. Optical sensor on the other side MPa in sodium chloride solutions with different measures the intensity of the light penetrating concentrations; 0 wt% (pure water), 3.5 wt% through the solution. When methane hydrates form (similar to seawater), 10 wt% and 20 wt%. on the free surface of solution exposed to the methane gas, the light is scattered by the methane hydrate crystals, and the light intensity detected EXPERIMENTS by the optical sensor sharply changes. On the other Apparatus hand, when the methane hydrate crystals dissoci The. apparatus used in this study consists of a ate, light intensity also sharply changes for the high-pressure hydrate cell of stainless steel where same reason. Therefore, the formation and disso methane hydrate is synthesized (Fig. 1). The hy ciation of methane hydrate can be detected by drate cell with a volume of about 100 ml is im measuring the change of light intensity. mersed in a water bath in which temperature is controlled by a heater and a refrigerator. The Procedures temperature of the solution in the cell is measured In this experiment, methane hydrates form from with a K-type thermocouple. The solution is agi the pressured methane gas and the sodium chlo tated by a magnetic stirrer. The pressure of meth ride solution in the hydrate cell. In the first place, ane gas is measured with a pressure gauge using the sodium chloride solution was added to the hy semi-conductor transducer. The cell has two glass drate cell until the surface of the solution was windows in the walls facing each other for visual observed through the window. Then, methane gas observation and optical detection of methane hy was pressed into the cell up to the starting pres drate formation and dissociation. sure by a compressor. The detector of formation and dissociation of The formation and dissociation of methane methane hydrate consists of a halogen lamp, an hydrate was regulated by changing the temperature optical sensor and an optical power meter. The of the solution after a constant volume of methane Optical Fiber Scope Thermocouple High-Pressure Valve Pressure Gauge Light Guide Cable Temperature-Controlled Water Bath Optical sensor / \ I `Sodium Chloride Solution Magnetic Stirrer Glass Windows Fig. 1. Schematic diagram of the experimental apparatus for hydrate studies. P-T conditions for CH4-hydrate dissociation in NaCI solutions 327 gas was sealed in the hydrate cell. The tempera tion were obtained for sodium chloride solutions ture in the hydrate cell was lowered to form with four different concentrations; 0 wt%, 3.5 methane hydrate, with a slight pressure decrease wt%, 10 wt% and 20 wt%. The results are shown by cooling. When the methane hydrate formed, in Fig. 2 together with previous results compiled the light intensity detected by the optical sensor by Sloan (1990). The conditions for methane hy sharply changed. The formation of methane hy drate dissociation in pure water determined by this drate was also confirmed by visual observation study agree well with the results from other stud using an optical fiber scope. The temperature was ies. Our results show that the dissociation pres raised after the formation of methane hydrate. sure of methane hydrate increases and the disso During the heating, the light intensity changed ciation temperature decreases as increasing the again and recovered to the original light intensity concentrations of sodium chloride in the solutions when methane hydrate dissociated. The condition (Kobayashi et al., 1951; de Roo et al., 1983). The for methane hydrate dissociation was determined data of this study agree well with those of by measuring the pressure and temperature at Kobayashi et al. (1951), although their data is which the change of light intensity occurred during slightly scattered due to the systematical overesti heating. mation of the stability of methane hydrate in so dium chloride solutions (Diamond, 1994). De Roo et al. (1983) have made similar ex RESULTSAND DISCUSSION periments in a pressure range up to 11 MPa and Conditions for methane hydrate dissociation in obtained an empirical equation to explain their sodium chloride solution results of methane hydrate dissociation in sodium The conditions for methane hydrate dissocia chloride solutions. Since their experiments were Temperature (K) 260 270 273 280 290 300 0 Owt% NaCI (this work) + 5 x 3.5wt% NaCI (this work) v + I Owt% NaCI (this work) 0 20wt% NaCI (this work) 10 a J Methane hydrate (Sloan,1990) N ++ X 1Owt% NaCI (Kobayashi et al.,1951) 20wt% NaCI (Kobayashi et al., 1951) U) 15 r W L 20 \ 25 I 1 l: 1 1 I Fig. 2. Pressure and temperature conditions for methane hydrate dissociation in sodium chloride solutions. Solid curves are fitted to Eq. (1) of methane hydrate dissociation conditions for respective concentrations of sodium chloride. a 328 T. Maekawa et al. performed using sodium chloride solutions with dissociation, p° is the atmospheric pressure [MPa], concentrations different from our experiments T is the temperature [K] of methane hydrate dis (11.7 wt%, 20.5 wt%, 21.6 wt% and 24.2 wt%), sociation, and x is the mole fraction of sodium their individual data are not compared in Fig. 2. chloride in the liquid phase. Our data agree well with the values calculated by Using the empirical equation, we can calculate their empirical equation in the pressure range up the difference in the dissociation temperature of to 11 MPa. However, their empirical equation methane hydrate between sodium chloride solu cannot be applied above 11 MPa. tion and pure water at any given pressure. The We obtained a new empirical equation by the dissociation temperature in 3.5 wt% sodium chlo least-squares method using our data together with ride solution is 1.1°C lower than that in pure wa the data for the methane-pure water system com ter up to 18 MPa. The result is similar to that of piled by Sloan (1990). The experimental data can Dholabhai et al. (1991) which was obtained by be described very well in the pressure range up to using synthetic seawater (salinity = 3.5%), and that 18 MPa by the following empirical equation: of Dickens and Quinby-Hunt (1994) using actual seawater (salinity = 3.35%). ln(p/p°) = -926 .815 + 31979.3/T + 144.909lnT + 5847.92x + 3220.26x2 Estimation of the depth of the base of methane + 5840.50 ln(1 x), (1) hydrate stability beneath seafloor It is important to estimate the maximum depth where p is the pressure [MPa] of methane hydrate of methane hydrate stability beneath seafloor to Temperature (K) 260 270 273 280 290 300 0 0 Stability Profile of Methane Water Temperature Hy drate in Pure Water Profile r+ CD 5 ;~_r J---- 500 0 CD 3 1000 2 10 Stability Profile of Methane Hydrate in 3.5wt%NaCI solution 15 .