Experimental loop system for fluidization exploitation of solid-state marine gas hydrate
US-10100264-B2 · Oct 16, 2018 · US
US10179884B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10179884-B2 |
| Application number | US-201614997304-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 15, 2016 |
| Priority date | Feb 22, 2013 |
| Publication date | Jan 15, 2019 |
| Grant date | Jan 15, 2019 |
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Disclosed are a device and a method for manufacturing a natural gas hydrate. Provided is the device for manufacturing a natural gas hydrate comprising: an ice slurry generation unit for preparing ice slurry having 13-20% of ice at normal pressure; a first pipe, having one end connected to the ice slurry generation unit for withdrawing the ice slurry from the ice slurry generation unit, and in which a high-pressure pump for increasing pressure on the ice slurry is interposed; a hydrate preparation reactor, which is connected to the other end of the first pipe so as to receive the pressurized ice slurry, and to which natural gas is supplied and mixed, for generating natural gas hydrate slurry; a second pipe, having one end connected to the hydrate preparation reactor, for withdrawing the natural gas hydrate slurry; and a dehydrating portion, which is connected to the other end of the second pipe, for dehydrating the natural gas hydrate slurry.
Opening claim text (preview).
What is claimed is: 1. A method for manufacturing natural gas hydrate, comprising: producing an ice slurry having 13-20% ice at normal pressure from water at a temperature above freezing point supplied from a raw water tank having the raw water stored therein and storing the ice slurry in an ice slurry generation unit; pressurizing the ice slurry discharged from the ice slurry generation unit with a high-pressure pump and injecting the pressurized ice slurry into a hydrate preparation reactor through a first pipe, and injecting natural gas into the hydrate preparation reactor; generating natural gas hydrate slurry by mixing the ice slurry and the natural gas in the hydrate preparation reactor; supplying the natural gas hydrate slurry prepared by the hydrate preparation reactor to a dehydrating portion through a second pipe; and separating the natural gas hydrate slurry into natural gas hydrate powder and water in the dehydrating portion, wherein the water separated by the dehydrating portion is returned to the ice slurry generation unit through a raw water recovering line for use in manufacture of the ice slurry, and wherein the raw water recovering line has a back pressure regulator interposed therein for maintaining a pressure of the dehydrating portion. 2. The method of claim 1 , wherein the high-pressure pump is configured to pressurize the ice slurry to 50-70 bar. 3. The method of claim 1 , wherein the hydrate preparation reactor comprises: a pipe having one end thereof connected to the first pipe and being horizontally disposed; and an agitator installed inside and along the pipe, wherein the natural gas hydrate slurry is prepared as the ice slurry and the natural gas pass through the pipe. 4. The method of claim 3 , wherein the hydrate preparation reactor further comprises a pressure sensor configured to measure a pressure inside the pipe, and wherein the pressure inside the pipe is measured by the pressure sensor, and the natural gas is supplied in such a way that the pressure inside the pipe is constant. 5. The method of claim 3 , wherein the hydrate preparation reactor further comprises a temperature sensor placed at the other end of the pipe and configured to measure a temperature of the natural gas hydrate slurry, and wherein an amount of the natural gas hydrate slurry discharged through the second pipe is controlled according to the temperature measured by the temperature sensor. 6. The method of claim 5 , wherein the amount of the discharged natural gas hydrate slurry is increased if the temperature measured by the temperature sensor is 4 degrees Celsius or higher, and the amount of the discharged natural gas hydrate slurry is decreased if the temperature measured by the temperature sensor is 2 degrees Celsius or lower. 7. The method of claim 1 , wherein the natural gas hydrate slurry generated by the hydrate preparation reactor has 10-15% of hydrate. 8. The method of claim 1 , wherein the dehydrating portion is configured to separate the natural gas hydrate slurry into powder and water having 90% of hydrate.
Recycling of a stream within the process or apparatus to reuse elsewhere therein · CPC title
Compressors or pumps · CPC title
Measuring or analysing fractions, components or impurities or process conditions during preparation or upgrading of a fuel · CPC title
Production of gas hydrates · CPC title
Mixing, stirring of fuel components · CPC title
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