IP Library Granted Patent US 10,816,140
Granted Patent B2
US 10,816,140 · App. 15/768,220 · Granted Oct 27, 2020

Method of an apparatus for treating boil-off gas for the purpose of supplying at least an engine

Inventor: David De Nardis (Beijing, CN)
Assignee: CRYOSTAR SAS
F17C7/04B63H21/38F17C7/00F17C9/02F17C2203/03F17C2205/0146F17C2221/033F17C2223/0161F17C2223/033F17C2227/0135F17C2227/0178F17C2265/03F17C2265/037F17C2265/066F17C2270/0105
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,816,140
App. No.
15/768,220
Granted
Oct 27, 2020
Kind
B2
Abstract

Apparatus for supplying natural gas fuel to an ocean-going tanker for the transport of liquefied natural gas (LNG), includes a first line with a compressor ( 12 ) having an inlet communicating with an ullage space ( 4 ) of at least one LNG storage tank ( 2 ) and an outlet communicating with a conduit leading from the compressor to at least one engine ( 38 ), and a second line with a forcing vaporiser ( 24 ) having an inlet communicating with a liquid storage region ( 6 ) of the tank ( 2 ), the second line being connected to the first line downstream of the compressor ( 12 ) and upstream of the at least one engine ( 38 ).

Claims (31)

1. A method for treating natural gas coming from an LNG tank for supplying at least an engine, comprising:

supplying a first line with natural boil-off gas;

compressing the natural boil-off gas to form compressed natural boil-off gas;

supplying a second line with liquefied natural gas;

forcing vaporization of the liquefied natural gas to form forced boil-off gas;

mixing said compressed natural boil-off gas with said forced boil-off gas to form a mixed gas, said mixed gas having a pressure of 10 to 20 bar; and

supplying at least an engine with the mixed gas at a pressure of 10 to 20 bar;

wherein the engine comprises a 2-stroke dual fuel Diesel engine or a 4-stroke dual fuel Diesel engine,

wherein said compressing of the natural boil-off gas is performed in two multi-stage compressors operating in parallel to form a first portion of compressed natural boil-off gas and a second portion of compressed natural boil-off gas, and

wherein said first portion of compressed natural boil-off gas and said second portion of compressed natural boil-off gas are at different pressures.

2. The method of claim 1 , wherein each of the two multi-stage compressors comprises six stages.

3. The method apparatus of claim 1 , wherein the first line comprises at least an after cooler positioned downstream of the compressing the natural boil-off gas, and the second line comprises at least a heater positioned downstream of the forced vaporization.

4. The method of claim 1 , further comprising cooling the compressed natural boil-off gas in the first line in an after cooler before mixing the compressed natural boil-off gas with the forced boil-off gas.

5. The method of claim 4 , further comprising heating the forced boil-off gas after the forced vaporization and before mixing the compressed natural boil-off gas with the forced boil-off gas.

6. The method of claim 1 , further comprising removing liquid after vaporization of the liquefied natural gas from fluid in the second line with a mist separation device.

7. The method of claim 1 , further comprising, after the forced vaporization, heating the forced boil-off gas in the second line.

8. The method of claim 1 , further comprising providing at least one storage tank containing a ullage space and a volume of liquefied natural gas, wherein said first line is in fluid communication with said ullage space and said second line is in fluid communication with said volume of liquefied natural gas.

9. The method according to claim 1 , wherein, prior to said mixing, said forced boil-off gas is passed through a phase separator vessel wherein liquid disengages from the forced boil-off gas.

10. The method according to claim 1 , wherein, prior to said mixing, said natural boil-off gas is passed through a phase separator vessel wherein liquid disengages from the natural boil-off gas.

11. The method of claim 1 , further comprising heating the mixed gas prior to being supplied to said at least an engine.

12. The method of claim 1 , further comprising cooling the natural boil-off gas in a spray precooler upstream of the compressor.

13. A method for treating natural gas coming from an LNG tank for supplying at least an engine, comprising:

supplying a first line with natural boil-off gas;

compressing the natural boil-off gas to form compressed natural boil-off gas;

supplying a second line with liquefied natural gas;

forcing vaporization of the liquefied natural gas to form forced boil-off gas;

mixing said compressed natural boil-off gas with said forced boil-off gas to form a mixed gas; and

supplying at least an engine with the mixed gas;

wherein the engine comprises a 2-stroke dual fuel Diesel engine or a 4-stroke dual fuel Diesel engine,

wherein said compressing of the natural boil-off gas is performed in two multi-stage compressors operating in parallel to form a first portion of compressed natural boil-off gas and a second portion of compressed natural boil-off gas, and

wherein said first portion of compressed natural boil-off gas and said second portion of compressed natural boil-off gas are at different pressures.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 27, 2018
From: DE NARDIS, DAVID
To: CRYOSTAR SAS
Reel/Frame 045651/0802 →
Continuity (1)
Related Publication 20180313497A1 · Nov 1, 2018
Cited By (3)
US 12,480,497 US 12,584,488 US 12,590,757