Experimental loop system for fluidization exploitation of solid-state marine gas hydrate
US-10100264-B2 · Oct 16, 2018 · US
US10351790B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10351790-B2 |
| Application number | US-201314768411-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 27, 2013 |
| Priority date | Jun 27, 2013 |
| Publication date | Jul 16, 2019 |
| Grant date | Jul 16, 2019 |
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The present invention provides an apparatus for molding gas hydrate pellets that includes: a pulverizer in which dehydrated gas hydrates are pulverized; a cooler having a rotating shaft provided therein, comprising a plurality of agitation blades installed along a height direction of the rotating shaft and configured to cool the gas hydrates to a predetermined temperature; a decompressor configured to decompress the cooled gas hydrates to a predetermined pressure; and a pellet molder configured to mold the decompressed gas hydrates to pellets.
Opening claim text (preview).
What is claimed is: 1. An apparatus for molding gas hydrate pellets, comprising: a dehydrating unit configured to remove moisture from a slurry state of gas hydrates to transform the slurry state of the gas hydrates to a cake state of the gas hydrates; a pulverizer in which the cake state of the gas hydrates is pulverized; a cooler having a rotating shaft provided therein, comprising a plurality of agitation blades installed along a height direction of the rotating shaft and configured to cool the pulverized gas hydrates to a predetermined temperature; a decompressor configured to decompress the cooled gas hydrates to a predetermined pressure; and a pellet molder configured to mold the decompressed gas hydrates to pellets, wherein the pulverizer is configured to pulverize and decrease effective diameters of the gas hydrates converted into the cake after the dehydrating, wherein the gas hydrates pulverized in the pulverizer to have the effective diameters decreased are supplied to the cooler, and wherein the pulverizer includes a fixed blade and a wing blade, and the gas hydrates injected into the pulverizer are pulverized by a compressive force between the fixed blade and the wing blade caused by rotation of the wing blade. 2. The apparatus of claim 1 , wherein the plurality of agitation blades have a different speed of rotation from one another. 3. The apparatus of claim 2 , further comprising a roller unit coupled to the rotating shaft and configured to frictionally roll against an inner circumferential surface of the cooler. 4. The apparatus of claim 3 , wherein the roller unit comprises: a pair of first rollers formed to be separated by 180 degrees about the rotating shaft; and a pair of second rollers, each overlapped partially with the pair of first rollers in a lengthwise direction of the rotating shaft, and formed to be separated by 180 degrees about the rotating shaft so as to have a phase difference of 90 degrees from the pair of first rollers along the inner circumferential surface of the cooler. 5. The apparatus of claim 4 , further comprising: a first roller support formed between the first roller and the rotating shaft and configured to support the first roller; and a second roller support formed between the second roller and the rotating shaft and configured to support the second roller, wherein the first roller support and the second roller support each comprise a roller spring so as to allow the first roller and the second roller to be in close contact with the inner circumferential surface of the cooler. 6. The apparatus of claim 5 , further comprising an agitation blade support formed between the plurality of agitation blades and the rotating shaft and configured to support the plurality of agitation blades, wherein a lubrication surface is formed between the agitation blade support and the rotating shaft, and wherein the first roller support, the second roller support and the agitation blade support, provided in plurality, are each connected with a bevel gear. 7. The apparatus of claim 6 , wherein the bevel gear formed above the first roller support and the bevel gear formed below the second roller support are each fixably coupled to the rotating shaft. 8. The apparatus of claim 1 , wherein the cooler further comprises: a cooling gas inlet formed at a lower portion of the cooler for injection of cooling gas; and a cooling gas outlet formed at an upper portion of the cooler for discharge of cooling gas to an outside. 9. The apparatus of claim 1 , further comprising a belt conveyor configured to transfer the decompressed gas hydrates to the pellet molder, wherein the belt conveyor is a mesh belt conveyor having a predetermined size of mesh. 10. The apparatus of claim 9 , further comprising a transfer part configured to receive the gas hydrates having passed the mesh of the belt conveyor and transfer the gas hydrates to the pellet molder. 11. The apparatus of claim 10 , wherein the belt conveyor has a direction thereof controlled toward the pellet molder or away from the pellet molder. 12. The apparatus of claim 10 , wherein the pellet molder comprises a briquetting machine, and wherein the transferred gas hydrates are molded by the briquetting machine to first pellets having a greater diameter than that of the gas hydrates. 13. The apparatus of claim 12 , further comprising a storage configured to collect and store second pellets collected when the belt conveyor is directed away from the pellet molder and the first pellets formed by the briquetting machine. 14. The apparatus of claim 1 , wherein the decompressor comprises: a decompression chamber having the cooled gas hydrates received therein for decompression; and a plurality of pressure tanks connected to the decompression chamber and each having a different pressure. 15. The apparatus of claim 14 , wherein the plurality of pressure tanks comprise: a first pressure tank; a second pressure tank having a lower pressure than the first pressure tank; a third pressure tank having a lower pressure than the second pressure tank; and a fourth pressure tank having a lower pressure than the third pressure tank. 16. The apparatus of claim 15 , wherein the fourth pressure tank is configured for maintaining atmospheric pressure and for having boil off gas (BOG) supplied thereto, the BOG being generated by the pellet molder. 17. The apparatus of claim 16 , wherein the fourth pressure tank, the third pressure tank and the second pressure tank are each configured to supply gas to the third pressure tank, the second pressure tank and the first pressure tank, respectively, if the fourth pressure tank, the third pressure tank and the second pressure tank each have a pressure that is greater than or equal to a predetermined value.
Molding or moulds · CPC title
Drying or removing water · CPC title
Production of gas hydrates · CPC title
Heat exchange, direct or indirect · CPC title
Mixing, stirring of fuel components · CPC title
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