Patent Application
20160115407
The present invention relates to the general field of odorizing natural gas, and more precisely it relates to a system and a method of injecting liquid odorant into a natural gas pipe.
Natural gas is odorless. Because of its potentially dangerous nature, present-day regulations require an odorant to be added in natural gas pipes in order to enable natural gas to be detected by means of its odor. This operation is generally performed using pure odorants or mixtures of odorants such as tetrahydrothiophene (designated by the acronym THT) or tert-butyl mercaptan (designated by the acronym TBM).
Systems for injecting odorant in liquid form into a natural gas pipe are generally dimensioned so as to be effective at the maximum observable gas flow rate at the point of injection. Nevertheless, when the real flow rate of gas becomes lower than the maximum flow rate, prior art systems for injecting odorant become less effective, which can lead to defective odorization of the gas.
Furthermore, such observed variations in the gas flow rate in pipes are particularly large when the maximum flow rate of gas to be odorized is small, as can occur in particular at points for injecting biomethane or at gas distribution stations. In addition, the opening up of gas markets to competition has led to ever increasing variability being observed in the amplitude and the frequency of the gas flow rates that can be observed, even at points for interconnecting large gas transport networks.
Various systems are known for odorizing natural gas. In particular there exist systems for injection by evaporation in which a portion of the gas for odorizing is diverted from the main flow and is put into contact with the liquid odorant, which it evaporates until thermodynamic equilibrium is reached. The diverted flow is then mixed with the main gas flow in order to obtain a mixture containing the desired odorant content.
Such evaporation systems require the supply of liquid odorant to be maintained at the same pressure as the gas flowing in the pipe, which can raise manifest problems with regulations. In addition, contact between the odorant and natural gas leads to the odorant being polluted, with it being possible for compounds in the gas to become dissolved in the odorant, thereby degrading its quality. Finally, the physical principle on which such systems are based leads to great variability in the contents of odorant in the gas if there is a change in ambient temperature (since saturated vapor pressure is a function of temperature). This physical principle is also very poorly adapted to using odorants that are made up of a mixture of chemicals, such as in particular TBM.
Another known system is that of systems using injection and a pump, in which liquid odorant is injected directly into the gas pipe by means of a diaphragm pump or by injecting odorant by means of gas under pressure. The liquid odorant evaporates in the gas by having recourse to an injection tube including a porous material, or after spraying coarse droplets.
Those injection and pump systems inject a fixed quantity of odorant each time the pump is activated. In particular, when the flow rate of gas in the pipe becomes very low, the frequency at which the pump is activated decreases, thereby leading to the system operating discontinuously. Unfortunately, the absence of back pressure between two successive actuations of the pump leads to the pump losing its priming if there is the slightest sealing defect in the pump. Furthermore, injecting a large quantity of odorant into a very low gas flow rate each time the pump is actuated leads to poor evaporation of the odorant.
A main object of the present invention is thus to provide a system and a method of injecting liquid odorant into a natural gas pipe that does not present the above-mentioned drawbacks.
In accordance with the invention, this object is achieved by a system for injecting liquid odorant into a natural gas pipe, the system comprising: a tank containing the odorant in liquid form; a high-pressure pump connected to the tank; a common injection manifold fed with liquid odorant by the high-pressure pump; a plurality of odorant injectors fed with liquid odorant under pressure by the common injection manifold for the purpose of injecting the odorant into the gas pipe so as to cause it to be atomized in the gas pipe; and an electronic injection computer for controlling the injectors and the high-pressure pump.
The pressure in the common injection manifold is maintained at a high value by the high-pressure pump. The pressure at which the odorant is injected at the outlet from an injector can thus be high, thereby optimizing odorant/gas mixing in the gas pipe. More precisely, by reducing the outlet section of the injectors and by using a high pressure at the outlet from the injectors, it is possible to increase the speed at which the liquid odorant is injected into the gas pipe. The speed difference between the flow of the natural gas in the gas pipe and the injection speed of the odorant leads to almost instantaneous atomization of the odorant when it is injected (the continuous jet of liquid odorant transforms into a mist of odorant droplets having a diameter of the order of a few micrometers). This leads to optimizing odorant/gas mixing.
Furthermore, controlling the injectors by an electronic injection computer makes it possible to control accurately the quantities of odorant that are injected, in particular as a function of the gas flow rate in the gas pipe. Likewise, the range of gas flow rates that can be “odorized” can be increased by subdividing the flow rate at which odorant is injected by using a plurality of injectors.
The pressurizing of the liquid odorant (by the high-pressure pump) may be physically separated from regulating the quantities of odorant that are injected (via injectors), thereby avoiding any loss of priming of the high-pressure pump associated with sealing defects.
In addition, the injection system invention is relatively compact compared with prior art injection systems, thus enabling it to be installed directly on the gas pipe, and possibly enabling a plurality of systems to be installed in parallel for odorizing high gas flow rates.
Preferably, the system further comprises a sensor for measuring the gas flow rate, connected to the electronic injection computer, and serving to measure the flow rate of gas flowing in the natural gas pipe upstream from the injectors. The injection system is thus made completely independent of external flow rate measurement, thus increasing its reliability.
Also preferably, the common injection manifold includes a pressure limiter device. Such a device makes it possible to control pressure in the common injection manifold, thereby avoiding any excess pressure in the injectors, which could lead to faulty operation.
The injectors may be electrohydraulic injectors controlled by solenoid valve or controlled by piezoelectric actuator. The system may further include a filter interposed between the tank and the high-pressure pump.
The injectors may be fastened to a common sleeve for mounting in a gas pipe via flange mounting. This simplifies installing such a system on a gas pipe and does not require any particular civil engineering work. Furthermore, the sleeve with its injectors can be manufactured in full in a factory, thereby facilitating both qualification testing and maintenance operations.
The invention also provides a method of injecting liquid odorant into a natural gas pipe, the method comprising: using a high-pressure pump to feed a common injection manifold with liquid odorant coming from a tank, said common injection manifold being connected to a plurality of injectors leading into a gas pipe; and using an electronic injection computer to control the injectors to inject a predetermined volume of liquid odorant into the gas pipe at a predetermined pressure so as to cause the odorant to be atomized in the gas pipe.
The common injection manifold may be fed with liquid odorant at a pressure lying in the range 200 bars to 2000 bars, and the gas pipe may be fed with natural gas at a pressure lying in the range one bar to 100 bars.
Other characteristics and advantages of the present invention appear from the following description made with reference to the accompanying drawings, which show an embodiment having no limiting character. In the figures:
The injection system 10 comprises in particular a tank 14 containing the odorant, which is present in liquid form. The liquid odorant is typically tetrahydrothiophene or thiophane (commonly designated by the acronym THT). Alternatively, it may be made up of tert-butyl mercaptan (designated by the acronym TBM) or of a mixture of these chemicals with each other or with other chemicals.
The tank 14 is connected to a high-pressure pump 16 with a filter 18 being interposed between these elements. The high-pressure pump is dimensioned so as to be capable of delivering the maximum needed flow rate at a pressure lying in the range 200 bars to 2000 bars, approximately.
The high-pressure pump 16 feeds a common injection manifold 20 continuously with liquid odorant under pressure. By way of example, this high-pressure pump 16 is a rotary pump known to the person skilled in the art.
The common injection manifold 20 is a hydraulic accumulator that constitutes a reserve of liquid odorant under high pressure. This manifold distributes the liquid odorant to a plurality of injectors 100 (there being four in this example) in uniform manner, i.e. the manifold feeds each of the injectors at the same pressure and with the same quantity of liquid odorant.
The injectors 100 serve to atomize the liquid odorant into the gas pipe 12 by the odorant vaporizing on coming into contact with the natural gas flowing in the gas pipe.
More precisely, the injectors 100 serve to inject a jet of liquid odorant into the gas pipe 12 that becomes transformed into an atomized spray, i.e. into a cloud of odorant droplets (having a diameter of the order of a few micrometers) thereby enhancing mixing of the odorant in the flow of natural gas.
More precisely, at the outlet from each injector, the jet of liquid odorant disintegrates immediately because of the very great difference in speed between the injected liquid and the natural gas flowing in the gas pipe (the odorant is said to be atomized).
As shown in
Furthermore, the injectors 100 may be regularly spaced apart angularly from one another over the entire circumference of the sleeve 22, so as to enable odorant to be injected as uniformly as possible.
An electronic injection computer 24 is electrically connected to the injectors 100 and to the high-pressure pump 16 in order to control them (via electrical connections 26 in
For this purpose, the injectors 100 are electrohydraulic injectors controlled by solenoid valves or controlled by piezoelectric actuators, thereby enabling the duration of injection and the exact quantity of odorant to be injected to be controlled electronically.
In known manner, the injector 100 is made up of two portions, namely a bottom portion 102 that constitutes the injector proper (often referred to as the nozzle), and a top portion 104 that constitutes the electrical control device of the injector.
Such an injector operates as follows. At rest, the injector is in a closed position as shown in
When the injector begins to open, the solenoid valve 106 is powered under the control of electrical pulses from the electronic injection computer 24. Its magnetic core compresses the return spring 108, which raises the ball 110 off its seat and thus allows leakage to take place towards the return circuit 124 (
When the injector is closed, the solenoid valve 106 ceases to be activated, so the return spring 108 pushes the magnetic core and drives the ball 110 against its seat in order to close the leaks. Pressure between the control chamber 112 and the pressure chamber 114 becomes balanced once again. The return spring 108 pushes the needle against its sealing bearing surface so as to shut the injection hole(s) 122.
Thus, the injector 100 operates like a solenoid valve, opening and closing very quickly in order to inject into the gas pipe the exact quantity of odorant that is set by the electronic injection computer 24. In particular, the flow rate of odorant injected by each injector depends on the pressure in the common injection manifold 20, on the length of time the needle 120 of the injector is open, and on the diameter of the injection hole(s) 122.
At the outlet from the injectors 100, the odorant in liquid form presents a pressure lying in the range 200 bars to 2000 bars, while the natural gas typically flows in the gas pipe 12 at a pressure lying in the range one bar to 100 bars. This large pressure difference, together with a small diameter for the injection hole(s) 122 of the injectors (typically in the range 0.1 millimeters (mm) to 0.2 mm), leads to a large difference in speed between the flow of natural gas in the gas pipe and the injection flow of odorant leaving the injectors. This speed difference leads to the odorant being atomized almost instantaneously on being injected into the gas pipe.
It should be observed that the injectors may be controlled by a piezoelectric actuator instead of a solenoid valve. Such a piezoelectric actuator is typically made up of a plurality of layers of quartz having the property of deforming on receiving an electrical pulse coming from the electronic injection computer. This enables injectors to be controlled particularly fast.
In order to ensure accurate control over the flow rate of odorant injected into the gas pipe 12, the electronic injection computer 24 receives information about the operation of the high-pressure pump 16 and of the common injection manifold 20 via electrical connections 28.
Likewise, it is advantageous to make provision for a sensor 30 to measure the gas flow rate in the gas pipe 12 upstream from odorant injection. By way of example, the sensor 30 may be an orifice plate, well known to the person skilled in the art for measuring a gas flow rate.
Such a sensor 30 is electrically connected via a connection 32 to the electronic injection computer 16 in order to inform it in real time about the flow rate of gas flowing in the gas pipe upstream from the injectors 100. The electronic injection computer can thus control accurately the quantities of odorant that are injected as a function of the gas flow rate in the gas pipe, and can adjust these quantities, in particular if the flow rate drops.
In another advantageous provision, the common injection manifold 20 includes a pressure limiter device 34. The function of the pressure limiter device is to control the pressure in the common injection manifold and to return the excess flow of odorant to the tank 14 via a controlled leak (connected to the return circuit 124).
In this variant embodiment, the injection system 10′ has a main gas pipe 12 that is split into a plurality of secondary pipes 12a (there being three of them in this example). Each secondary gas pipe 12a has its own liquid odorant injection module 200 (each module has a high-pressure pump, a common injection manifold, and an electronic injection computer, not shown in
Each injection module 200 is connected to the same liquid odorant tank (not shown in figure) and to a plurality of injectors 100 leading into the corresponding secondary gas pipe. Upstream from the injectors, a sensor 30 is provided in each secondary gas pipe 12a for measuring the gas flow rate (e.g. an orifice plate).
Such a system makes it possible to enlarge the range over which odorization is effective by allowing natural gas to flow through and be odorized in a plurality of secondary gas pipes as a function of the flow rate of natural gas through the system. In addition, since the injection modules 200 are independent of one another, they can take over from one another, when necessary.
| Number | Date | Country | Kind |
|---|---|---|---|
| 1355338 | Jun 2013 | FR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/FR2014/051398 | 6/10/2014 | WO | 00 |
