초록 ▼

Systems and processes that facilitate the absorption of natural gas or methane through the interaction of moderate pressure and low temperature into a liquid or liquid vapor medium for storage and transport, and back into a gas for delivery to market. In a preferred embodiment, the absorptive proper

Systems and processes that facilitate the absorption of natural gas or methane through the interaction of moderate pressure and low temperature into a liquid or liquid vapor medium for storage and transport, and back into a gas for delivery to market. In a preferred embodiment, the absorptive properties of ethane, propane and butane under moderate conditions of temperature and pressure (associated with a novel mixing process) are utilized to store natural gas or methane at more efficient levels of compressed volume ratio than are attainable with natural gas alone under similar holding conditions. The preferred mixing process efficiently combines natural gas or methane with a solvent medium such as liquid ethane, propane, butane, or other suitable fluid, to form a concentrated liquid or liquid vapor mixture suited for storage and transport. The solvent medium is preferably recycled in the conveyance vessel on unloading of the natural gas.

대표청구항 ▼

What is claimed is: 1. A process of mixing natural gas with a hydrocarbon solvent to yield a liquid medium suited for storage and transport at greater storage densities than compressed natural gas at the same storage conditions, comprising: cooling natural gas and a solvent to temperatures in a ran

What is claimed is: 1. A process of mixing natural gas with a hydrocarbon solvent to yield a liquid medium suited for storage and transport at greater storage densities than compressed natural gas at the same storage conditions, comprising: cooling natural gas and a solvent to temperatures in a range from below-40° F. to about-80° F., wherein the solvent is a liquid hydrocarbon, combining a flow stream of the natural gas having a molar flow rate with a flow stream of the liquid hydrocarbon solvent having a molar flow rate determined as a function of the molar flow rate of the flow stream of the natural gas causing a phase change of the combined flow streams of the natural gas and the liquid hydrocarbon solvent into a single phase liquid medium of natural gas absorbed in the hydrocarbon solvent, compressing the single phase liquid medium at pressures in a range of about 1200 psig to about 2150 psig, and storing the single phase liquid medium in a storage vessel, wherein the natural gas of the single phase liquid medium is stored at storage densities that exceed storage densities of compressed natural gas for the same pressure and temperatures. 2. The process of claim 1 wherein the compressing step includes compressing the liquid medium at pressures in a range of about 1200 psig to about 1440 psig. 3. The process of claim 2 wherein the cooling step includes cooling the gas and solvent to temperatures in a range from below-40° F. to about-60° F. 4. The process of claim 1 wherein the cooling step includes cooling the flow streams of natural gas and hydrocarbon solvent to temperatures in a range from below-40° F. to about-60° F. 5. The process of claim 1 wherein the hydrocarbon solvent is ethane. 6. The process of claim 1 wherein the hydrocarbon solvent is propane. 7. The process of claim 1 wherein the hydrocarbon solvent is butane. 8. The process of claim 1 wherein the natural gas is methane. 9. The process of claim 1 further comprising the steps of reducing the pressure of the single phase liquid medium of natural gas absorbed in the hydrocarbon solvent to separate the natural gas and hydrocarbon solvent, and heating the natural gas to gasify the natural gas. 10. The process of claim 9 further comprising the step of maintaining the liquid medium at a pressure of 1440 psig or less and at temperatures in a range from below-40° F. to-60° F. or above prior to reducing the pressure of the liquid medium. 11. The process of claim 9 further comprising the step of maintaining the liquid medium at a pressure of 1440 psig or less and at temperatures in a range from below-40° F. to-80° F. or above prior to reducing the pressure of the liquid medium. 12. The process of claim 9 further comprising the step of maintaining the liquid medium at a pressure of 2150 psig or less and at temperatures in a range from below-40° F. to-60° F. or above prior to reducing the pressure of the liquid medium. 13. The process of claim 9 further comprising the step of maintaining the liquid medium at a pressure of 2150 psig or less and at temperatures in a range from below-40° F. to-80° F. or above prior to reducing the pressure of the liquid medium. 14. The process of claim 9 further comprising the step of storing the hydrocarbon solvent in liquid phase for future use. 15. The process of claim 4 wherein the storage densities of the natural gas of the single phase liquid medium are in a volumetric ratio range of 215 ft3/ft3 to 335 ft3/ft3. 16. The process of claim 4 wherein the hydrocarbon solvent is ethane and wherein the storage densities of the natural gas of the single phase liquid medium are in a volumetric ratio range of 226 ft3/ft3 to 326 ft3/ft3. 17. The process of claim 4 wherein the hydrocarbon solvent is propane and wherein the storage densities of the natural gas of the single phase liquid medium are in a volumetric ratio range of 265 ft3/ft3 to 320 ft3/ft3. 18. The process of claim 4 wherein the hydrocarbon solvent is butane and wherein the storage densities of the natural gas of the single phase liquid medium are in a volumetric ratio range of 215 ft3/ft3 to 335 ft3/ft3. 19. The process of claim 4 wherein the storage densities of the natural gas of the single phase liquid medium are at least 1.23 to 1.66 times greater than that of compressed natural gas under the same temperature and pressure. 20. The process of claim 4 wherein the hydrocarbon solvent is ethane and wherein the storage densities of the natural gas of the single phase liquid medium are at least 1.23 to 1.36 times greater than that of compressed natural gas under the same temperature and pressure. 21. The process of claim 4 wherein the hydrocarbon solvent is propane and wherein the storage densities of the natural gas of the single phase liquid medium are at least 1.40 to 1.66 times greater than that of compressed natural gas under the same temperature and pressure. 22. The process of claim 4 wherein the hydrocarbon solvent is butane and wherein the storage densities of the natural gas of the single phase liquid medium are at least 1.33 to 1.43 times greater than that of compressed natural gas under the same temperature and pressure.