Patent Application
20220154885
This application claims the benefit of priority under 35 U.S.C. § 119 (a) and (b) to French Patent Application No. 2011856, filed Nov. 19, 2020, the entire contents of which are incorporated herein by reference.
The present invention relates to a method for vaporizing a liquid, particularly for vaporizing methane or some other liquid that vaporizes at a temperature below 0° C.
In the case of vaporizing a cryogenic liquid in an exchanger, if the regulation of the vaporization is not sufficiently precise, the hot end of the exchanger may be weakened as a result of excessive cold, which may damage it.
It is an object of this invention to reduce the risk of weakening by detecting deficiency of the regulation system and by modifying the regulation system in order to reduce the risk of weakening.
One subject of the invention provides a method for vaporizing a liquid in a heat exchanger in which a liquid vaporizes in the heat exchanger to form a gas which in normal operation is sent to a user through a first pipe, wherein if the rate of change of the rate of flow of liquid sent to the exchanger exceeds a threshold, the first pipe is closed and fluid, which may be gas vaporized in the heat exchanger and/or liquid not vaporized in the exchanger, is discharged into the atmosphere or to the flare stack through a second pipe and a valve, the opening of the valve being regulated by the fluid flow rate measured in the second pipe.
According to other optional aspects:
Another aspect of the invention provides an apparatus for vaporizing a liquid comprising a heat exchanger in which a liquid vaporizes to form a gas, a first pipe for sending the gas formed to a user in normal operation, a second pipe connected to the heat exchanger to send gas vaporized in the heat exchanger and/or liquid not vaporized in the exchanger to the atmosphere or to a flare stack, a detector for detecting whether the rate of change of the rate of flow of liquid sent to the exchanger exceeds a threshold, first regulating means for regulating the opening of a valve in the second pipe according to the flow rate measured in the second pipe, second regulating means for regulating the opening of a valve in the second pipe according to the pressure of the gas formed downstream of the heat exchanger, and means allowing the valve to be connected selectively to the first and to the second regulating means.
According to other optional aspects:
For a further understanding of the nature and objects for the present invention, reference should be made to the following detailed description, taken in conjunction with the accompanying drawings, in which like elements are given the same or analogous reference numbers and wherein:
The gas pipe 7 is connected to the pipes 9 and 11 that allow the gas to be sent to two different places: to a user in the case of the pipe 9, and to the atmosphere or to a flare stack in the case of the pipe 11. The pressure in the pipe 7 is regulated by the valve PV 1 controlled by the pressure controller PIC A.
In the event of poor operation of the valve FV 1 or flowmeter FI 1, it is possible to send the vaporized gas to the atmosphere or to a flare stack via the pipe 11 upstream of the valve PV 1 that regulates the pipe 7. In that case, the valve PV 2 on the pipe 11 is opened by the pressure controller PIC B, the setpoint of which is slightly higher than that of PIC A.
Optionally, a flowmeter FI 3 measures the gas flow rate in the pipe 9 to determine how much gas is sent to the user.
If the regulating system is deficient, a flow of liquid may reach the hot end of the exchanger 3, at the risk of weakening same. This arrival of liquid at the hot end may increase the pressure at the hot end of the exchanger 3, which means that the valves PV 1 and PV 2 open, thus increasing the risk of weakening through excessive cold.
A heat exchanger 3 allows a liquid 5 to be vaporized through counterflow exchange of heat with a fluid 1. The flow rate of the liquid 5 is regulated by the valve FV 1, controlled by FIC 1. The liquid 5 may be methane or any liquid that vaporizes at a temperature below 0° C. The liquid 5 vaporizes in the exchanger 3 to form the gas in the pipe 7.
The gas pipe 7 is connected to the pipes 9 and 11 that allow the gas to be sent to two different places: to a user in the case of the pipe 9, and to the atmosphere or to the flare stack in the case of the pipe 11. The pressure in the pipe 7 is regulated by the valve PV 1 controlled by the pressure controller PIC A.
In the event of poor operation of the valve PV 1, it is possible to send the vaporized gas to the atmosphere or to the flare stack via the pipe 11 upstream of the valve PV 1 that regulates the pipe 7. In that case, in normal operation, the valve PV 2 on the pipe 11 is opened by the pressure controller PIC B, the setpoint of which is slightly higher than that of PIC A.
Optionally, a flowmeter FI 3 measures the gas flow rate in the pipe 9 to determine how much gas is sent to the user.
If the regulating system FIC 1 is deficient, the rate of change of the rate of flow of liquid 5 increases beyond a threshold. This change in rate beyond the threshold is detected by the detector FDSHH which is connected to the pipe for the liquid 5.
According to the invention, if a rate of change of flow rate 5 is observed, the pipe 9 is closed and the sending of fluid to the atmosphere or to the flare stack is regulated according to the flow rate of fluid in the pipe 11.
Once it has been observed that this rate of change is particularly high, the system may enact the following changes:
Optionally, when the valve PV 1 is closed, its solenoid, if there is one, is also closed.
If the value of FI 3 is used in the calculations, its value is fixed at the last measured value and then reduced to 0 as the valve PV 1 closes.
As illustrated in the figure, it may be necessary to provide a valve FV 2 in parallel with the valve PV 2. Such is the case when the valve PV 2 would otherwise be too large to allow fine regulation of the flow passing through the exchanger 3. The valve FV 2 is sized to allow the nominal flow rate to pass.
In that case, the valve PV 2 is controlled by the pressure controller PIC B according to the pressure in the pipe 7, and the valve FV 2 is controlled by the flow rate controller FIC 2 according to the flow rate in the pipe 7 or 11.
If the rate of change of flow rate to a rate level with the threshold is detected by the detector FDSHH then, in this case, rather than the valve PV 2 being controlled by the FIC 2 instead of by the PIC B, the valve PV 2 will be closed and the valve FV 2 will be opened by the FIC 2, with a flow rate setpoint corresponding to that of FIC 1.
This principle may be applied whatever the mode via which the valve FV 1 is controlled. In the example, the flow rate controller FIC 1 is used but the valve on the pipe 5 may also or as an alternative be regulated according to the pressure or according to a level. It may be regulated manually. However, the presence of a flowmeter is needed in order to detect the poor operation of the vaporization by observing that the flow rate 5 is changing particularly rapidly.
It will be understood that many additional changes in the details, materials, steps and arrangement of parts, which have been herein described in order to explain the nature of the invention, may be made by those skilled in the art within the principle and scope of the invention as expressed in the appended claims. Thus, the present invention is not intended to be limited to the specific embodiments in the examples given above.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2011856 | Nov 2020 | FR | national |
