6 research outputs found

    Molecular Storage of Ozone in a Clathrate Hydrate: An Attempt at Preserving Ozone at High Concentrations

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    <div><p>This paper reports an experimental study of the formation of a mixed O<sub>3</sub>+ O<sub>2</sub>+ CO<sub>2</sub> hydrate and its frozen storage under atmospheric pressure, which aimed to establish a hydrate-based technology for preserving ozone (O<sub>3</sub>), a chemically unstable substance, for various industrial, medical and consumer uses. By improving the experimental technique that we recently devised for forming an O<sub>3</sub>+ O<sub>2</sub>+ CO<sub>2</sub> hydrate, we succeeded in significantly increasing the fraction of ozone contained in the hydrate. For a hydrate formed at a system pressure of 3.0 MPa, the mass fraction of ozone was initially about 0.9%; and even after a 20-day storage at −25°C and atmospheric pressure, it was still about 0.6%. These results support the prospect of establishing an economical, safe, and easy-to-handle ozone-preservation technology of practical use.</p> </div

    The initial ozone fraction in the formed hydrate versus the gas-phase composition.

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    <p>The mole fraction of ozone, <i>X</i><sub>O3</sub>, shown here is for the gas phase inside the reactor when the hydrate formation ceased. The legend inserted in the graph indicates the system pressure <i>p</i> during each hydrate-forming operation. The error bar for each data point represents the uncertainty of the ozone-fraction measurement by iodometry.</p

    Results of the ozone preservation tests.

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    <p>This graph shows the time evolution of ozone fraction (mass basis) in each O<sub>3</sub>+ O<sub>2</sub>+ CO<sub>2</sub> hydrate stored under an aerated atmospheric-pressure (0.101 MPa) condition temperature-controlled at −25°C. The comparison of the ozone preservation test data obtained in this study (marked by closed symbols) and those from a previous study <a href="http://www.plosone.org/article/info:doi/10.1371/journal.pone.0048563#pone.0048563-Nakajima1" target="_blank">[7]</a> (marked by open symbols) are compared. The legend inserted in the graph indicates the O<sub>3</sub>+ O<sub>2</sub> versus CO<sub>2</sub> molar ratio in the feed gas and the system pressure <i>p</i> for each hydrate-forming operation. The error bar for each data point represents the uncertainty of the ozone-fraction measurement by iodometry.</p

    Engineering Investigation of Hydrogen Storage in the Form of Clathrate Hydrates: Conceptual Design of Hydrate Production Plants

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    This paper describes a part of our feasibility study on the storage of hydrogen in the form of clathrate hydrates. The specific objective of this paper is to present conceptual designs of hydrogen-hydrate production plants applicable to large-scale in situ storage of hydrogen produced in an industrial complex area or to smaller-scale urban-area storage of hydrogen which is to be transported from the industrial complex area by container trucks. The plants were so designed as to produce either a simple hydrogen hydrate under a pressure of 35 MPa and a temperature of 140 K or a mixed hydrogen + tetrahydrofuran hydrate under a pressure of 30 MPa and a temperature of 223 K. In either case, the rate of hydrogen uptake into the hydrates during their production in each plant was targeted for 3000 Nm<sup>3</sup>/h (for use in an industrial complex area) or 500 Nm<sup>3</sup>/h (for use in an urban area). For each type of plant, we have prepared a process flow diagram accompanied by material-balance, heat-balance, and machinery specifications. The energy consumption in plant operation has also been evaluated, assuming that the cool energy generated by adjacent LNG facilities may or may not be available for cooling the hydrate-forming assemblies in each plant

    PXRD profile of an O<sub>3</sub>+ O2+ CO<sub>2</sub> hydrate at 98 K.

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    <p>The solid curve shows the intensities observed using Cu−Kα radiation. The top row of tick marks represent the calculated peak positions for the structure I hydrate, and the lower two rows represent those for the hexagonal ice Ih and cubic ice Ic, respectively. The hydrate sample (accompanied by ice crystals) used in this PXRD measurement was formed from a mixture of O<sub>3</sub>+ O2 and CO<sub>2</sub> in a nearly 2∶ 8 molar ratio at the condition of <i>p</i> = 2.0 MPa and <i>T</i> = 0.1°C.</p

    Schematic illustration of the experimental setup for forming the O<sub>3</sub>+ O<sub>2</sub>+ CO<sub>2</sub> hydrates.

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    <p>This setup consists of (a) an oxygen cylinder, (b) a carbon-dioxide cylinder, (c) an ozone generator, (d) a gas-mixing chamber, (e) a pressure gauge, (f) and (g) pressure gauges, (h) and (i) gas-pressurizing chambers, (j) a gas-sampling chamber, (k) a pressure gauge, (l) a hydrate-forming reactor, (m) a Pt-wire resistance thermometer, (n) a stirrer, (o) a data logger, (p) an immersion cooler, (q) a PID-controlled heater, (r) a vacuum pump, (s) an ozone monitor, (t) a vacuum pump, and (u) an ozone decomposer.</p
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