Gas supply system for high- and low-pressure gas-consuming apparatuses and method of controlling such a system

Patent metadata

Field	Value
Publication number	US-11898520-B2
Application number	US-202318192882-A
Country	US
Kind code	B2
Filing date	Mar 30, 2023
Priority date	Mar 31, 2022
Publication date	Feb 13, 2024
Grant date	Feb 13, 2024

Abstract

A system supplies gas to a high-pressure gas-consuming apparatus and a low-pressure gas-consuming apparatus of a floating structure including a tank. The supply system includes: a first supply circuit, a second supply circuit, a return line, a first heat exchanger and a second heat exchanger. The return line includes a flow-regulating member. The supply system includes a device for managing the supply system which includes a control module to control the flow-regulating member based on the characteristics of the gas.

First claim

The invention claimed is:

1. A system for supplying gas to at least one high-pressure gas-consuming apparatus and at least one low-pressure gas-consuming apparatus of a floating structure comprising at least one tank configured to contain the gas, the supply system comprising:
at least one first circuit supplying gas to the high-pressure gas-consuming apparatus,
at least one high-pressure evaporator configured to evaporate the gas circulating in the first gas supply circuit,
at least one second circuit supplying gas to the low-pressure gas-consuming apparatus, comprising at least one compressor configured to compress gas taken in a vapor state into the tank to a pressure compatible with the requirements of the low-pressure gas-consuming apparatus,
at least one gas return line connected to the second supply circuit downstream of the compressor and extending to the tank,
at least one first heat exchanger and one second heat exchanger, each configured to exchange heat between the gas circulating in the return line in the vapor state and the gas circulating in the first supply circuit in a liquid state, the first supply circuit comprising a pump interposed between the first heat exchanger and the second heat exchanger, the return line comprising a flow-regulating member arranged between the first heat exchanger and the tank, and
a management device configured to manage said supply system, said management device comprising at least one first sensor and a first detector respectively configured to determine a temperature and pressure of the gas present in the first supply circuit between the first heat exchanger and the pump, a second sensor configured to determine a temperature of the gas present in the first supply circuit between the tank and the first heat exchanger, a third sensor configured to determine a temperature of the gas present in the return line between the first heat exchanger and the flow-regulating member, the management device comprising a control module configured to control the flow-regulating member according to the characteristics of the gas determined by the first sensor, the second sensor, the third sensor and the first detector.

2. The supply system according to claim 1 , further comprising a fluid analyzer configured to determine a composition of the gas in the liquid state contained in the tank.

3. The supply system according to claim 1 , wherein the management device comprises a second detector configured to determine a pressure of the gas present in the tank, the control module being configured to control the flow-regulating member according to the pressure of the gas determined by the second detector.

4. The supply system according to claim 1 , wherein the return line comprises a flowmeter configured to determine the flow rate of gas in the vapor state circulating in the return line, the control module being configured to control the flow-regulating member according to the gas flow rate determined by the flowmeter.

5. The supply system according to claim 1 , wherein the first supply circuit comprises at least one pumping member configured to pump the gas taken from the liquid state in the tank.

6. A method for controlling the supply system according to claim 1 , comprising:
comparing the temperature of the gas present in the first supply circuit between the first heat exchanger and the pump, and a maximum temperature threshold determined as a function of the pressure of the gas present in the first supply circuit between the first heat exchanger and the pump, a composition of the gas circulating in the supply system and a safety margin,
reducing, when the temperature of the gas present in the first supply circuit between the first heat exchanger and the pump is greater than the maximum temperature threshold, a passage section of the flow-regulating member,
implementing, when the temperature of the gas present in the first supply circuit between the first heat exchanger and the pump is lower than the maximum temperature threshold, a comparison between the temperature of the gas present in the return line between the first heat exchanger and the flow-regulating member and an optimal temperature threshold determined according to the temperature of the gas present in the first supply circuit between the tank and the first heat exchanger and a temperature difference,
reducing, when the temperature of the gas present in the return line between the first heat exchanger and the flow-regulating member is greater than the optimal temperature threshold, the passage section of the flow-regulating member,
increasing, when the temperature of the gas present in the return line between the first heat exchanger and the flow-regulating member is lower than the optimal temperature threshold, the passage section of the flow-regulating member.

7. The control method according to claim 6 , wherein the control method is repeated over time.

8. The control method according to claim 6 , wherein the supply system further comprises a fluid analyzer configured to determine a composition of the gas in the liquid state contained in the tank, and the composition of the gas is determined by the fluid analyzer.

9. The control method according to claim 6 , wherein the composition of the gas is determined by technical documentation.

10. The control method according to claim 6 , wherein the maximum temperature threshold is determined by virtue of a data table of several types of gas.

11. The control method according to claim 6 , wherein the safety margin and the temperature difference correspond to a value between 1° C. and 3° C.

12. The control method according to claim 6 , wherein the management device comprises a second detector configured to determine a pressure of the gas present in the tank, the control module being configured to control the flow-regulating member according to the pressure of the gas determined by the second detector, and the pressure of the gas determined by the second detector is compared to a pressure threshold.

13. The control method according to claim 12 , further comprising interrupting the gas flow within the return line when the pressure of the gas determined by the second detector is lower than the pressure threshold.

Assignees

• Gaztransport Et Technigaz

Inventors

• Moussaoui Selma
• Aoun Bernard
• Narme Romain

Classifications

• F02M31/183 Primary

  Control · CPC title

• F02M25/089

  Layout of the fuel vapour installation · CPC title

• F17C9/04 Primary

  Recovery of thermal energy · CPC title

• B63H21/38 Primary

  Apparatus or methods specially adapted for use on marine vessels, for handling power plant or unit liquids, e.g. lubricants, coolants, fuels or the like ({in outboard drives B63H20/001; } lubricating or cooling machines or engines in general F01 - F04) · CPC title

• F17C6/00

  Methods and apparatus for filling vessels not under pressure with liquefied or solidified gases · CPC title