Abstract
A three-phase, pilot-scale continuous-jet hydrate reactor (CJHR) has been developed for the production of gas hydrates. The reactor receives water and a hydrate-forming species to produce the solid gas hydrate. The CJHR has been tested for the production of CO2 hydrate for the purpose of ocean carbon sequestration. Formation of CO2 hydrate was investigated using various reactor/injector designs in a 72-l high-pressure vessel. Designs of the CJHR varied from single-capillary to multiple-capillary injectors that dispersed (1) liquid CO2 into water or (2) water into liquid CO2. The novel injector is designed to improve the dispersion of one reactant into the other and, thus, eliminate mass transfer barriers that negatively affect conversion. An additional goal was an increase in production rates of two orders of magnitude. The designed injectors were tested in both distilled and saline water. Hydrate production experiments were conducted at different CO2 and water flow rates and for pressures and temperatures equivalent to intermediate ocean depths (1100-1700 m). The pilot-scale reactor with the novel injection system successfully increased hydrate production rates and efficiency.
Original language | English |
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Pages (from-to) | 71-77 |
Number of pages | 7 |
Journal | Chemical Engineering Journal |
Volume | 135 |
Issue number | 1-2 |
DOIs | |
State | Published - Jan 15 2008 |
Funding
Gratefully acknowledged is support by the Ocean Carbon Sequestration Program, Office of Biological and Environmental Research, U.S. Department of Energy under Contract No. DE-AC05-00OR22725 with UT-Battelle, LLC. The authors are thankful to Dr. Tommy Phelps for stimulating discussions and helpful comments, and to Dr. M.K. Savage for editing the manuscript.
Funders | Funder number |
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Ocean Carbon Sequestration Program | |
U.S. Department of Energy | DE-AC05-00OR22725 |
Biological and Environmental Research |
Keywords
- Carbon dioxide hydrate
- Gas hydrate reactor
- Ocean carbon sequestration