Egbert
Leonardus, Stewart
Robert
Bruce
, V.
| 1. | Method of compressing combustible gas flowing through a conduit having an inlet end and an outlet end and being provided with a nonreturn inlet valve arranged at its inlet end and with an openended tubular arranged coaxially in the conduit which tubular has a crosssectional area which is smaller than the cross sectional area of the conduit, which method comprises the steps of (a) allowing combustible gas to enter into the conduit through the nonreturn inlet valve; (b) supplying oxidant to the combustible gas in the tubular, the amount of oxidant being equal to the amount of oxidant required to combust at least part of the combustible gas in the tubular; (c) allowing the mixture of combustible gas and oxidant to ignite in the tubular, which ignition yields a high pressure wave front closing the nonreturn inlet valve and pushing gas out of the tubular and a low pressure wave front; and (d) allowing the nonreturn inlet valve to open on arrival of the low pressure wave front, followed by steps (a) through (d) . |
| 2. | Apparatus for carrying out the method of compressing combusti¬ ble gas according to claim 1, comprising a conduit having an inlet end and an outlet end, a nonreturn inlet valve arranged at the inlet end of the conduit, an openended tubular arranged coaxially in the conduit downstream of the nonreturn inlet valve, a localized ignition source arranged in the tubular, and an oxidant supply debouching into the tubular, wherein the crosssectional area of the tubular is smaller than the crosssectional area of the conduit and wherein an annular passage is defined between the tubular and the conduit. |
| 3. | Apparatus according to claim 2, wherein the nonreturn inlet valve is provided with a control device allowing opening the inlet valve at a predetermined pressure difference. |
| 4. | Method of compressing combustible gas flowing through a conduit substantially as described in the specification with reference to the accompanying drawing. |
The present invention relates to compressing combustible gas flowing through a conduit. An example of such combustible gas is natural gas.
A suitable application of the present invention is downhole compression of natural gas, this is done to enhance the production from an underground natural gas reservoir. Natural gas is produced from an underground reservoir containing natural gas through a tubing arranged in a well drilled to the reservoir. During produc¬ tion, the cumulative amount of natural gas produced increases and consequently the reservoir pressure will decrease. As a result of the decrease in reservoir pressure the production rate decreases and, in order to maintain the production rate at an economically acceptable level the gas has to be compressed and suitably gas is compressed downhole. This downhole gas compression will result in an increased economic cumulative production.
An alternative application of the present invention is com¬ pression of natural gas flowing through a pipeline to increase the rate of natural gas transported through the pipeline.
USA patent specification No. 2 899 287 discloses a method of compressing an oxidant-containing gas flowing through a conduit provided with a tubular arranged coaxially in the conduit which tubular has an inlet end and an outlet end and is provided with a non-return inlet valve at its inlet end. The known method comprises the steps of (a) supplying fuel into the tubular;
(b) allowing oxidant to enter into the tubular through the non-return inlet valve;
(c) allowing the mixture of fuel and oxidant to ignite, which ignition yields a high pressure wave front closing the non-return
inlet valve and pushing gas out of the outlet end of the tubular and a low pressure wave front; and
(d) allowing the non-return inlet valve to open on arrival of the low pressure wave front, followed by steps (a) through (d) .
In the known method the pressure increase for the compression stage is very small, the pressure at the outlet end of the conduit is about 2 or 3% above the pressure at the inlet end. For pumping natural gas such a pressure increase for a compression stage is unacceptably small. Therefore it is an object of the present
10 invention to provide a method of compressing a combustible gas which will yield a much larger pressure increase per compression stage.
To this end the method according to the invention of compress¬ ing combustible gas flowing through a conduit having an inlet end
* ■ - and an outlet end and being provided with a non-return inlet valve arranged at its inlet end and with an open-ended tubular arranged coaxially in the conduit which tubular has a cross-sectional area which is smaller than the cross-sectional area of the conduit comprises the steps of - Q (a) allowing combustible gas to enter into the conduit through the non-return inlet valve;
(b) supplying oxidant to_the combustible gas in the tubular, the amount of oxidant being equal to the amount of oxidant required to combust at least part of the combustible gas in the tubular; - (c) allowing the mixture of combustible gas and oxidant to ignite, which ignition yields a high pressure wave front closing the non-return inlet valve and pushing gas out of the tubular and a low pressure wave front; and
(d) allowing the non-return inlet valve to open on arrival of
30 the low pressure wave front, followed by steps (a) through (d) .
Applicant has found that to obtain a large pressure increase it is required to let the combustible gas flow intermittently through the conduit so that the high pressure wave front is fully utilized to push the gas out of the tubular allowing to entrain the combus¬
35 tible gas passing through the annular space.
The invention further relates to an apparatus for carrying out the method of compressing combustible gas which apparatus comprises a conduit having an inlet end and an outlet end, a non-return inlet valve arranged at the inlet end of the conduit, an open-ended tubular arranged coaxially in the conduit downstream of the non¬ return inlet valve, a localized ignition source arranged in the tubular, and an oxidant supply debouching into the tubular, wherein the cross-sectional area of the tubular is smaller than the cross-sectional area of the conduit and wherein an annular passage *-0 is defined between the tubular and the conduit.
The invention will now be described by way of example in more detail with reference to the accompanying drawing showing schemat¬ ically a cross-sectional view of the apparatus for carrying out the method of compressing combustible gas according to the invention. J - 5 Th apparatus 1 for compressing combustible gas comprises a conduit 3 having an inlet end 5 and an outlet end 8, which conduit 3 is provided with a non-return inlet valve 10 arranged at the inlet end 5 of the conduit 3.
In the conduit 3 is arranged coaxially an open-ended tubular 13
20 downstream of the non-return inlet valve 10. The open-ended tubular 13 is fixed in the conduit 3 by means of struts 15. The cross- sectional area of the open-ended tubular 13 is smaller than the cross-sectional area of the conduit 3 so that an annular passage 17 is defined between the outer wall of the open-ended tubular 13 and
25 the inner wall of the conduit 3.
The apparatus 1 furthermore comprises an oxidant supply 18 of which the outlet opening 19 debouches into the open-ended tubular 13, and a localized ignition source 20 arranged in the open-ended tubular 13 downstream of the outlet opening 19 of the oxidant
30 supply 18. The localized ignition source 20 is connected to a supply of electric power (not shown) for allowing the source 20 to glow.
The apparatus 1 is arranged in a pipe for transporting combus¬ tible gas, for example the apparatus 1 is arranged in a tubing (not
shown) arranged in a well through which natural gas can rise from the bottom of the well to surface.
During normal operation natural gas flows through the tubing and enters the apparatus 1 through the non-return inlet valve 10 arranged at the inlet end 5 of the conduit 3. The gas flows through the annular space 17 and through the open-ended tubular 13. Oxidant is supplied to the combustible gas in the open-ended tubular 13, wherein the amount of oxidant is sufficient to combust at least part of the combustible gas in the open-ended tubular 13. Suitably the amount of oxidant equals the amount of oxidant required to combust the combustible gas in the open-ended tubular 13.
Electric power is supplied to the localized ignition source 20 and the mixture of combustible gas and oxidant is allowed to ignite in the open-ended tubular 13. This ignition yields a high pressure wave front closing the non-return inlet valve 10 and pushing gas out of the open-ended tubular 13 and a low pressure wave front. The gas flowing out of the open-ended tubular 13 entrains gas flowing through the annular space 17.
The amount of gas combusted in the open-ended tubular 13 is smaller than the total amount of combustible gas flowing through the conduit 3.
Upon arrival of the low pressure wave front at the non-return inlet valve 10, the non-return inlet valve 10 opens allowing natural gas to enter into the apparatus 1, and the above described sequence of steps starts again to compress the natural gas.
When the localized ignition source 20 is sufficiently heated, the localized ignition source acts as a hot spot so that supply of electric power can be interrupted.
The oxidant is a gas containing free oxygen, an example of suitable oxidant is air, a further example is air enriched with oxygen. The oxidant can furthermore contain water, which upon vaporizing in the open-ended tubular 13 will furthermore increase the pressure.
The non-return inlet valve 10 can be provided with a control device (not shown) allowing opening of the non-return inlet valve 10 at a pre-determined pressure difference across the valve. An
example of the control device is a spring, another example is a magnetic latch.
It will be appreciated that more than one apparatus according to the present invention can be arranged in series, each following apparatus compressing the gas compressed by the previous one. If required, the compressed gas can be cooled between two successive compression stages.
The conduit 3 has a constant inner diameter; in an alternative embodiment of the invention, the conduit comprises in the direction of flow a narrowing section, a section having a constant diameter (in which section the open-ended tubular is arranged) and a widen¬ ing section.
Next Patent: COMPRESSING GAS FLOWING THROUGH A CONDUIT