Apparatus for producing hydrate slurry

• US 7,541,009 B2
• Filed: 03/14/2003
• Issued: 06/02/2009
• Est. Priority Date: 05/31/2002
• Status: Expired due to Fees

• Current Assignee: JFE Engineering Corporation (JFE Holdings Incorporated)
• Original Assignee: JFE Engineering Corporation (JFE Holdings Incorporated)
• Inventors: Takao, Shingo, Matsumoto, Shigenori, Furumoto, Naoyuki, Ogoshi, Hidemasa
• Primary Examiner(s): Bhat; Nina
• Application Number:
  US10/514,981
• Publication Number:
  US 20050163681A1
• Time in Patent Office: 2,272 Days
• Field of Search: 422/198, 62/541, 624/34
• US Class Current: 422/198
• CPC Class Codes: F24F 5/0017 using cold storage bodies, e.g. ice
• CPC Class Codes: F25B 2315/003 Hydrates for sorption cycles
• CPC Class Codes: F25B 25/005 using primary and secondary systems
• CPC Class Codes: F25B 5/02 arranged in parallel
• CPC Class Codes: F25D 17/02 for circulating liquids, e.g. brine
• CPC Class Codes: F28F 13/125 by stirring
• CPC Class Codes: Y02E 60/14 Thermal energy storage

Abstract

An apparatus produces hydrate slurry, which is a mixture of aqueous solution and hydrate, by cooling aqueous solution containing a guest compound, which generates the hydrate at temperature higher than 0° C., by using a cooling medium. The apparatus includes a first heat exchanger for supercooling the aqueous solution while holding the aqueous solution in a liquid state and in a second heat exchanger, which is provided on the downstream side of the first heat exchanger for cooling hydrate slurry.

Claims

1. An apparatus for generating a hydrate slurry, wherein the hydrate slurry is a mixture of an aqueous solution containing a guest compound and a hydrate of the guest compound, the hydrate being generated by cooling the aqueous solution at a temperature of more than 0°

C.,

the apparatus comprising a first heat exchanger, at least one second heat exchanger and a canceling device,

the first heat exchanger being configured for supercooling the aqueous solution to generate a supercooled aqueous solution, while holding the aqueous solution in a liquid state,

the canceling device being provided on the downstream side of the first heat exchanger, the canceling device being configured to cancel the supercooling of the aqueous solution, and

the at least one second heat exchanger being provided on the downstream side of the first heat exchanger, the at least one second heat exchanger being configured to cool the hydrate slurry generated from the aqueous solution, the supercooling of which is canceled by the canceling device.

2. The apparatus according to claim 1, wherein the at least one second heat exchanger comprises a plurality of second heat exchangers which are switchable.

3. The apparatus according to claim 2, wherein when adhesion of the hydrate is detected in a second heat exchanger of the plurality of the second heat exchangers in which the hydrate slurry is generated, the generation of the hydrate slurry is stopped in said second heat exchanger, the adhered hydrate is melted therein, and the hydrate slurry is generated in another second heat exchanger of the plurality of the second heat exchangers.

4. The apparatus according to claim 2, wherein the plurality of the second heat exchangers are switched over successively at a fixed time interval within which hydrate which becomes adhered is melted.

5. The apparatus according to claim 1, wherein the canceling device comprises a device for introducing the hydrate slurry into the supercooled aqueous solution supercooled by the first heat exchanger.

6. The apparatus according to claim 5, wherein the supercooled aqueous solution has a supercooling degree of 0.7°

C. or more.

7. The apparatus according to claim 5, wherein the hydrate slurry introduced into the supercooled aqueous solution is in an amount of 1 vol % or more of the total amount of the supercooled aqueous solution.

8. The apparatus according to claim 5, wherein the hydrate slurry introduced into the supercooled aqueous solution is in an amount of 1.8 vol % or more of the total amount of the supercooled aqueous solution.

9. The apparatus according to claim 5, wherein the supercooled aqueous solution has a Reynolds number of 4500 or more.

10. The apparatus according to claim 5, wherein the hydrate slurry introduced into the supercooled aqueous solution is generated by the at least one, second heat exchanger.

11. The apparatus according to claim 5, wherein the hydrate slurry introduced into the supercooled aqueous solution is accommodated in a thermal storage tank for the hydrate slurry.

12. The apparatus according to claim 1, wherein the canceling device is selected from the group consisting of a cooling portion of a small refrigerating machine, a low-temperature protrusion, an oscillating portion of an ultrasonic oscillator, a low-frequency oscillator, a static mixer, a mixing blade and a pump.

13. The apparatus according to claim 1, wherein the guest compound is at least one compound selected from the group consisting of tetra-n-butyl ammonium salt, tetra-iso-amyl ammonium salt, tetra-n-butyl phosphonium salt and tetra-iso-amyl sulfonium salt.

14. In an apparatus for generating a hydrate slurry containing a hydrate of a guest compound produced by cooling an aqueous solution containing the guest compound at a temperature of higher than 0°

C., the apparatus comprising;

a refrigerator configured to cool a refrigerant and provide a cooled refrigerant, the refrigerator having a plurality of evaporators, the plurality of evaporators being provided so as to be switchable and the cooled refrigerant flowing in one or more of the plurality of evaporators;

a circulation system configured to cool the aqueous solution of the guest compound by the cooled refrigerant in one or more of the plurality of the evaporators;

a controller configured to (i) stop the cooling of the aqueous solution of the guest compound in one evaporator of the plurality of the evaporators, when a blockage of the circulation system occurs due to a hydrate which is generated by the cooling thereof, and (ii) start the cooling of the aqueous solution of the guest compound in another evaporator of the plurality of evaporators; and

a device for supplying the refrigerant at a high temperature from the refrigerator to the evaporator in which the cooling of the aqueous solution of the guest compound is stopped so as to melt the hydrate causing the blockage of the circulation system.

15. The apparatus according to claim 14, further comprising a detector configured to detect the blockage of the circulation system.

16. The apparatus according to claim 15, wherein the detector is at least one detector selected from the group consisting of (i) a flowmeter provided on an outlet pipe of one evaporator of the plurality of evaporators, (ii) a thermometer provided on an outlet pipe of one evaporator of the plurality of evaporators and (iii) a differential pressure gauge provided across an inlet pipe and an outlet pipe of the one evaporator of the plurality of evaporators.

17. The apparatus according to claim 14, wherein the refrigerator is an absorption refrigerating machine having an absorber and has a device for supplying the refrigerant in a gaseous state generated by the generator to the evaporator of the plurality of evaporators in which the cooling of the aqueous solution of the guest compound is stopped.

18. The apparatus according to claim 14, wherein the refrigerator is a compression refrigerating machine having a compressor and a device for supplying the refrigerant in a gaseous state generated by the compressor to the evaporator of the plurality of evaporators in which the cooling of the aqueous solution of the guest compound is stopped.

19. The apparatus according to claim 14, wherein the refrigerator is a compression refrigerating machine having a condenser and a device for supplying the refrigerant in a liquid state generated by the condenser to the evaporator of the plurality of evaporators in which the cooling of the aqueous solution of the guest compound is stopped.

20. The apparatus according to any one of claims 14 to 19, wherein the aqueous solution of the guest compound is supercooled by one or more of the plurality of the evaporators;

and a canceling device is located on an outlet pipe of said one or more of the plurality of evaporators so as to cancel the supercooling of the aqueous solution.

21. The apparatus according to claim 20, wherein the canceling device is selected from the group consisting of a cooling portion of a small refrigerating machine, a low-temperature protrusion, an oscillating portion of an ultrasonic oscillator, a low-frequency oscillator, hydrate slurry injecting means, a static mixer, a mixing blade and a pump.

22. The apparatus according to any one of claims 14 to 19, wherein the guest compound is at least one compound selected from the group consisting of tetra-n-butyl ammonium salt, tetra-iso-amyl ammonium salt, tetra-iso-butyl phosphonium salt and tri-iso-amyl sulfonium salt.