Page 238 - Handbook Of Multiphase Flow Assurance
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Hydrate stability and crystal growth            237






























            FIG. 10.12  Schematic of the apparatus.

            Experimental equipment and procedure for methane hydrate
              A schematic of the experimental equipment is given in Fig. 10.12. The apparatus was built
            around a stainless steel spherical cell of 5.08 cm internal diameter rated for 10.1 MPa. The cell
            was filled with 150 stainless steel balls of 0.31 cm diameter, needed for surface renewal. A
            Thermolyne orbital shaker with 0.4 cm amplitude was used to agitate the stainless steel balls
            inside the cell at 16.7 rps. A cylinder of 99.9% pure methane from Matheson Inc. was used as
            a gas supply without further purification. The volumetric unit and the vent chamber shown
            on the diagram were not used in this set of experiments. Pressure was monitored via Heise
            gauges rated at 13.43 and 2.01 MPa. A Barocel differential electronic manometer (0.267 MPa
            full scale, 0.133 Pa resolution) was used at low pressures. A grease-sealed glass flask attached
            to the water and hydrocarbon inlet was used to vacuum distill water into the steel cell.
              The cell was immersed in an 8 l Neslab ethanol stirred bath. The bath was cooled using the
            Neslab cryocool CC-100 II 2-stage immersion cooler. The minimal attainable temperature was
            180 K. The operating temperature was maintained with the Neslab temperature controller
            with ±0.3 K stability at temperatures below 260 K and ±0.1 K at higher temperatures and a
            600 W immersion heater. Temperatures were measured with an Omega platinum resistance
            thermometer with ±0.1 K accuracy. The shaker frequency was selected to provide maximum
            cell agitation without excessive vibration.
              The lines and cell were evacuated to 4 Pa. Water (degassed, deionized) was vacuum distilled
            into the cell which was partially immersed in liquid N 2 . After the vacuum distillation process
            was complete, lines were re-evacuated. The bath was set to a constant experimental temperature.
              Fig. 10.13 presents a schematic of the experimental procedure. The gas was admitted into
            the system, and 8–10 min were allowed for pressure and thermal equilibrium without agitat-
            ing the cell. After the system had stabilized, the shaker was started and the pressure drop was
            monitored as hydrates formed.
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