The present invention relates to flares for burning waste gas and, more particularly, to a flare gas system for burning a plurality of flare gases, e.g., high pressure and low pressure flare gases.
At oil and gas well sites, particularly where drilling is conducted in shale formations, there is an array of equipment, as for example tank batteries to collect crude oil and/or distillates from the oil and gas wells, as well as separators to separate gas/water from hydrocarbons. Generally speaking, tank batteries are a source of low pressure flare gas while separators are a source of high pressure flare gas. Low pressure flare gases typically have a pressure less than about 50 psig while high pressure flare gas can have a pressure of from 50 to 1500 psig In either event, the gases cannot be allowed to accumulate as the pressure build up could create hazards to humans as well as potential damage to equipment. Nor can they be vented to atmosphere for environmental reasons. To alleviate this problem, these gases, both high and low pressure, are vented from the equipment and flared using a suitable flare gas assembly.
In one aspect, the present invention relates to a flare gas system for burning a plurality of flare gases.
In yet another aspect, the present invention relates to a flare gas system which can flare a plurality of flare gases, wherein one of the gases may be low pressure gas.
In a further aspect, the present invention relates to a method of flaring of a plurality of flare gases.
These and further features and advantages of the present invention will become apparent from the following detailed description, wherein reference is made to the figures in the accompanying drawings.
The flare gas system of the present invention is designed to accommodate the flaring of a plurality of flare gases which can include high pressure and low pressure flare gases. To this end, the flare gas system of the present invention has at least one flare gas assembly which can accommodate both high and low pressure gases and at least two flare gas assemblies for high pressure flare gases. While the system will be described with respect to the use of two high pressure flare gas assemblies, it will be understood that three or more such flare gas assemblies can be employed if necessary. In any event, the flare gas assemblies are married together to form at least one embodiment of the present invention.
Turning first to
As can be seen from the drawings, the system can be fabricated, in part, from various sizes of pipe and conduit, the needed connections being made by way of bolt flanges shown as 30 in
Turning now to
As can be seen from
Disposed in annulus 50 is a flow restrictor 60, flow restrictor 60 comprising an annular plate through which extend a plurality of orifices, the orifices being aligned axially with annulus 50. While as shown restrictor 60 has substantial height relative to wall thickness, in point of fact, the height or thickness of flow restrictor 60 can be as little as ¼″ and thus can be easily fabricated by drilling holes through an annular plate. It is to be noted that the orifices in restrictor 60, while shown as axially aligned with annulus 50, could be angled so as to impart a swirling motion in chamber 54.
Flare gas assemblies 14 and 16 are fully described in U.S. patent application Ser. No. 17/167,541, the disclosure of which is incorporated herein by reference for all purposes. Suffice it to say that flare gas assemblies 14 and 16 comprise a tubular housing 62 in which is reciprocally mounted a spring biased valve element 64, valve element 64 being mounted on a shaft 66.
In operation, and generally speaking, high pressure flare gas would be introduced into annulus 50 via flare gas feed line 22. Low pressure flare gas would be typically introduced into annulus 42 via flare gas feed line 24, and a third flare gas would be introduced into annulus 46 via flare gas feed line 20. It will be understood however that the flare gases introduced into the various annuli could all be high pressure, low pressure, or intermediate pressure. However, in a preferred case, high pressure flare gas is introduced into annulus 50 so that it passes through flow restrictor 60 and imparts momentum to the air/flare gas mixture in chamber 54. Additionally, typically a low pressure gas would be introduced into annulus 42 so as to be mixed in chamber 54 by combustion air issuing from air conduit 26. Further, high pressure gas in annulus 50 also flows into pressure operated variable orifice flare gas assemblies 14 and 16.
Turning now to
Turning now to
Gas handler 78 forms a first plenum 78A and a second plenum 78B. Gas handler 78 basically comprises an upper wall 104, a lower wall 106, an intermediate wall 107, and a peripheral wall 108. As can be seen, flare gas feed line 80 is in open communication with first plenum 78A, while flare gas feed line 84 is in open communication with second plenum 78B. Plenum 78A is in open communication with annulus 100 in which is disposed a flow restrictor 60 described above with respect to the embodiments of
In a typical operation, high pressure flare gas is fed into plenum 78A where it would pass both into annulus 100 through flow restrictor 60 and into flare gas assemblies 74 and 76. Low pressure flare gas would typically be introduced into annulus 92 via flare gas feed line 82, and a third flare gas would be introduced via flare gas feed line 84 in plenum 78B into annulus 94. Thus, the high pressure flare gas would both flow through the restrictor 60 and into the pressure operated variable orifice flare gas assemblies comprising flare gas assemblies 74 and 76. The combined flare gases issuing from annuli 92, 96, and 100 are mixed with combustion air from air pipe 26 in chamber 54 and ignited by igniter 31.
One feature of the present invention is that a single igniter, e.g., igniter 31 can ignite the flare gases emanating from flare gas assembly 72 as well as flare gas assemblies 74 and 76. This is at least partially due to the novel arrangement of flow restrictor 60 which increases the velocity of the flare gas issuing from annulus 100 and effects cross-lighting of not only the lower pressure flare gas assembly 72 but flare gas assemblies 74 and 76 as well.
Although specific embodiments of the invention have been described herein in some detail, this has been done solely for the purposes of explaining the various aspects of the invention, and is not intended to limit the scope of the invention as defined in the claims which follow. Those skilled in the art will understand that the embodiment shown and described is exemplary, and various other substitutions, alterations and modifications, including but not limited to those design alternatives specifically discussed herein, may be made in the practice of the invention without departing from its scope.
This application is a continuation-in-part of U.S. application Ser. No. 16/108,534 filed on Aug. 22, 2018, which in turn is a continuation-in-part of U.S. Ser. No. 15/587,960 filed May 5, 2017, which in turn claims the benefit of provisional U.S. Ser. No. 62/403,301 filed Oct. 3, 2016, and provisional 62/332,811 filed May 6, 20216; and this application is a continuation-in-part of U.S. application Ser. No. 17/167,541 filed on Feb. 4, 2021, all the disclosures above being incorporated herein by reference for all purposes.
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Number | Date | Country | |
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62403301 | Oct 2016 | US | |
62332811 | May 2016 | US |
Number | Date | Country | |
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Parent | 17167541 | Feb 2021 | US |
Child | 17227673 | US | |
Parent | 16108534 | Aug 2018 | US |
Child | 17167541 | US | |
Parent | 15587960 | May 2017 | US |
Child | 16108534 | US |