Patent Publication Number: US-11045762-B2

Title: Systems and methods for accurate measurement of gas from wet gas wells

Description:
PRIORITY 
     This application is a non-provisional continuation application of U.S. patent application Ser. No. 15/259,275, filed Sep. 8, 2016, and published as U.S. Pat. Pub. No. 2017-0065932, which itself is a non-provisional application of and claims priority to and the benefit of U.S. Prov. App. Ser. No. 62/215,191, filed Sep. 8, 2015, the entire disclosures of which are expressly incorporated here by reference. 
    
    
     BACKGROUND 
     Field 
     Embodiments of the disclosure relate to systems and methods for accurate measurement of gas recovered from a gas well. Specifically, embodiments relate to accurate measurement of wet gas recovered from a gas well using a venturi meter. 
     Description of the Related Art 
     Venturi meters are widely used to measure the flow rates of gases, including single-phase gas flow rates of natural gas recovered from gas reservoirs. These meters provide accurate gas flow measurements at the early stages during the life of a gas well, when the well is producing dry gas with a small amount of liquid, such as less than about 5% by volume. However, as reservoirs become mature, the wells start to “cut” or produce more liquid, such as water or other condensate, with the gas. This can occur as the reservoir temperature and pressure decline with production. Liquid present with the gas affects the accuracy of gas flow rate measurement by venturi meters. Additional liquid in the recovered natural gas leads to inaccurate production monitoring, allocation, and reservoir engineering and management decisions. 
     Nearly all existing gas-producing wells are equipped with venturi meters to measure gas flow rates. However, using multiple venturi meters to correct for the inaccuracies caused by increased liquid cut is expensive and requires significant infrastructure modifications to existing and new pipeline systems. Existing methods to correct for increased liquid cut are expensive and require a number of modifications and additions to existing systems and require frequent calibrations. 
     SUMMARY 
     Applicant has recognized that there is a need for accurate and efficient measurement of natural gas flow rates from wet gas wells. The proposed systems and methods are efficient and do not require any modifications to existing venturi meters other than adding a liquid knockout drum ahead of the venturi meter. One advantage of this technology is utilizing the existing infrastructure without doing any major ground work by installing a knockout surge tank ahead of the existing venturi meter to knock out the liquid that is being produced with the gas. In certain embodiments of the disclosure, no additional liquid storage tanks or new, separate flow lines are required. 
     The disclosure presents the methodology for correcting the erroneous readings of venturi meters for measuring gas flow rates when liquid is being produced from gas wells along with natural gas. The proposed systems and methods take advantage of existing infrastructure in proximity to the venturi meters and are designed to be retrofitted to knock out the liquid before the venturi meter. Any knocked out liquid fluid, such as water or other condensate, is then recombined into the gas flow after the venturi meter without the need for a compressor or additional flow line to carry away the liquid. 
     A simple, retrofitable modification is proposed to improve the accuracy of the wet gas flow measurements using existing venturi meters. The technique is quick to apply due to the ready set up and lay-out of existing gas wells, which serves the purpose of applying the recommended technology to have accurate gas rate measurements. The proposed systems and methods are straightforward to implement and require minimal maintenance. The systems and methods are very practical as well, since the venturi meter is located ahead of a choke valve, which allows for knock out of liquid fluids and potential condensates due to the differential pressure across the choke. 
     Liquid fluid, such as water, or other potential condensates can form in the gas stream. Liquid that is being knocked out in a knockout drum, or surge tank, can be pumped back to the flow-line downstream of the choke by pressurizing the liquid in the tank using higher gas pressure upstream of the choke. In some embodiments, the knockout drum has a check valve to allow liquids to flow out of the tank, and thus bypass the venturi meter. The check valve will not allow liquid to be carried through the venturi meter by flowing natural gas. This results in having only dry gas passing through the venturi meter, and this will result in more accurate gas flow rate measurements. The systems and methods also avoid having external means such as compressors to pump out the liquid that is being accumulated in the knockout drum. 
     Systems and methods of the present disclosure lead to accurate gas measurements for wet gas wells and more accurate and reliable gas rate allocations, which aid in both production and reservoir management, and also in planning studies. 
     Embodiments of the disclosure include a liquid removal system for increasing accuracy of gas flow meters. The system includes a liquid knockout drum, the liquid knockout drum operable to receive a natural gas feedstream comprising wet gas, the liquid knockout drum further comprising: an impingement plate, where the impingement plate is disposed proximate to the natural gas feedstream, and is operable to remove liquids from the natural gas feedstream; a drum separator, where the drum separator separates a first portion of the liquid knockout drum from a second portion of the liquid knockout drum, the drum separator operable to collect the liquids removed from the natural gas feedstream by the impingement plate; and a check valve, where the check valve is disposed between the first portion of the liquid knockout drum and the second portion of the liquid knockout drum proximate the drum separator, and the check valve is operable to allow one way liquid fluid communication from the first portion of the liquid knockout drum to the second portion of the liquid knockout drum when the check valve is an in open state. 
     The system further includes a dry gas outlet line in fluid communication between the first portion of the liquid knockout drum and a gas flow meter, where the dry gas outlet line is operable to allow dry gas flow from the liquid knockout drum to the gas flow meter; a pressurized line comprising dry gas in fluid communication with the second portion of the liquid knockout drum, the pressurized line operable to drive liquids in the second portion of the liquid knockout drum through a liquid outlet line; and a manifold line, where the manifold line is operable to recombine dry gas from the dry gas outlet line and liquids from the liquid outlet line. 
     In some embodiments, the system further comprises a choke valve disposed between the gas flow meter and the manifold line. In other embodiments, the system further comprises a valve between the pressurized line comprising dry gas and the second portion of the liquid knockout drum. Still in other embodiments, the system comprises a valve between the second portion of the liquid knockout drum and the manifold line. In yet other embodiments, the gas flow meter is a venturi meter. 
     Still in other embodiments, the impingement plate is disposed between about 0.1 m and about 1 m away from the natural gas feedstream comprising wet gas, and the impingement plate comprises a forward face disposed facing toward the natural gas feedstream, where the forward face is larger than an inlet cavity of the natural gas feedstream comprising wet gas. In some embodiments, the check valve is operable to remain closed as the liquids collect around the drum separator, and is operable to open responsive to a level of the liquids collecting proximate the drum separator reaching a predetermined level. In other embodiments, a diameter of the gas flow meter is less than a diameter of the dry gas outlet line. 
     In certain embodiments, diameters of the pressurized line comprising dry gas and the liquid outlet line are less than diameters of the dry gas outlet line and manifold line. In some embodiments, the valve between the pressurized line comprising dry gas and the second portion of the liquid knockout drum and the valve between the second portion of the liquid knockout drum and the manifold line are operable to open responsive to the check valve opening. 
     Additionally disclosed is a method for liquid removal to increase accuracy of gas flow meters, where the method comprises the steps of contacting a natural gas feedstream comprising wet gas with an impingement plate and separating liquids from the natural gas feedstream to produce a dry gas stream and aggregated liquids. The method further includes the steps of collecting the aggregated liquids from the natural gas feedstream; measuring a flow rate of the dry gas stream; pressurizing the collected aggregated liquids with a portion of the dry gas stream after measuring the dry gas stream; and flowing the collected aggregated liquids and the portion of the dry gas stream to a common line. 
     Some embodiments of the method further comprise the step of recombining the aggregated liquids and the portion of the dry gas stream with a remaining portion of the dry gas stream, where the remaining portion of the dry gas stream is not used to pressurize the aggregated liquids. In other embodiments of the method, the step of separating liquids from the natural gas feedstream further comprises the step of utilizing a liquid knockout drum, the liquid knockout drum operable to receive the natural gas feedstream comprising wet gas. 
     Still in other embodiments, the step of collecting the aggregated liquids from the natural gas stream further comprises the step of accumulating the aggregated liquids at a drum separator, where the drum separator separates a first portion of the liquid knockout drum from a second portion of the liquid knockout drum. In yet other embodiments, the step of collecting the aggregated liquids from the natural gas feedstream further comprises the step of actuating a check valve, where the check valve is disposed between the first portion of the liquid knockout drum and the second portion of the liquid knockout drum proximate the drum separator, and where the check valve is operable to allow one way liquid fluid communication from the first portion of the liquid knockout drum to the second portion of the liquid knockout drum when the check valve is an in open state. 
     In some embodiments of the method, the step of pressurizing the aggregated liquids further comprises the step of opening a valve disposed between a gas flow meter and the second portion of the liquid knockout drum. Still in other embodiments, the step of recombining the aggregated liquids and the portion of the dry gas stream with the remaining portion of the dry gas feed stream further comprises the step of opening a valve between the second portion of the liquid knockout drum and the common line. 
     In certain embodiments, the step of measuring the flow rate of the dry gas stream further comprises the step of utilizing a venturi meter. Still in other embodiments, the method includes the step of disposing the impingement plate between about 0.1 m and 1 m away from the natural gas feedstream comprising wet gas, with a forward face disposed facing toward the a natural gas feedstream, where the forward face is larger than an inlet cavity of the natural gas feedstream comprising wet gas. 
     In some embodiments, the step of actuating a check valve check further comprises maintaining the check valve in a closed position as aggregated liquids collect around the drum separator, and opening the check valve responsive to a predetermined level of aggregated liquids collecting proximate the drum separator. In other embodiments, the step of measuring the flow rate of the dry gas stream further comprises flowing the dry gas stream through a portion of pipe with a reduced diameter. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       These and other features, aspects, and advantages of the present disclosure will become better understood with regard to the following descriptions, claims, and accompanying drawings. It is to be noted, however, that the drawings illustrate only several embodiments of the disclosure and are therefore not to be considered limiting of the disclosure&#39;s scope as it can admit to other equally effective embodiments. 
         FIG. 1  is schematic diagram of one embodiment of a liquid knockout system for a wet gas well. 
         FIG. 2  provides perspective views of example impingement plates for use in embodiments of the present disclosure. 
         FIG. 3  provides a flow chart for one exemplary method of liquid knockout for a wet gas well. 
     
    
    
     DETAILED DESCRIPTION 
     So that the manner in which the features and advantages of the embodiments of systems and methods for accurate measurement of gas from wet gas wells, as well as others, which will become apparent, may be understood in more detail, a more particular description of the embodiments of the present disclosure briefly summarized previously may be had by reference to the embodiments thereof, which are illustrated in the appended drawings, which form a part of this specification. It is to be noted, however, that the drawings illustrate only various embodiments of the disclosure and are therefore not to be considered limiting of the present disclosure&#39;s scope, as it may include other effective embodiments as well. 
     To make use of existing venturi meters for accurate gas flow measurements in the presence of liquid, such as water or other fluids, without doing any extensive infrastructure modifications, systems and methods are proposed to accurately measure only gas phase flow, without having liquid fluid impact the accuracy of the venturi meters. Embodiments comprise a knockout surge tank, also referred to as a liquid knockout drum, that will be installed upstream of the venturi meter allowing only gas with minimal liquid contents to pass through the meter. 
     The trapped liquid in the liquid knockout drum will be reintroduced back into the gas flow line downstream of the venturi meter by pressure and a choke valve, by pressurizing the liquid knock out drum using the line pressure between the venturi meter and the choke valve. The proposed liquid knockout drum will be equipped with a splashing mechanism, also referred to as an impingement plate, to have dry gas moving upward passing through the venturi meter and liquid, such as water and other fluids, being dropped to the bottom of the tank. The liquid knockout drum is also equipped with a check valve to allow liquid to flow to the bottom of the tank, while preventing the liquid from flowing back to the gas stream upstream of the venturi meter. 
     Liquid that is knocked out of the wet gas stream in the tank can be pumped back to the dry gas flow line downstream of the choke by pressurizing the liquid in the liquid knockout tank using line pressure upstream of the choke. Only substantially dry gas that is substantially free of liquid fluid passes through the venturi meter, and this leads to accurate gas rate measurements. This also will avoid having some external means, such as compressors, to pump out the liquid that is being accumulated in the liquid knockout drum. As the liquid will be reintroduced in the same gas flow line downstream of the choke valve and venturi meter, no additional line or storing and handling infrastructure of the knocked-out liquid will be needed. 
     Substantially dry gas or dry gas, as referred to in this specification, refers to gas in which the flow can be accurately measured by a single-phase gas flow meter, such as a venturi meter. Single-phase gas flow meters, such as venturi meters, can be calibrated to measure the gas flow within accuracy requirements if the amount of liquid fluid in the gas stream is less than about 6% by volume. If the liquid fluid in the gas stream is greater than about 6% by volume, the error in the gas flow rate obtained from single-phase gas flow meters falls into an unacceptable accuracy range. Substantially wet gas or wet gas, as referred to in this specification, refers to gas in which the flow cannot be accurately measured by a single-phase gas flow meter, such as a venturi meter. 
     Referring now to  FIG. 1 , a schematic diagram is shown of one embodiment of a liquid knockout system for a wet gas well. Liquid knockout system  100  includes a feedstream  102  from a gas well producing wet gas. A feedstream comprising wet gas can include wet gas from a newly-drilled gas well, a mature gas well, or can include wet gas produced from a combination of gas wells, such as newly-drilled and mature gas wells. Liquid knockout system  100  further includes a liquid knockout drum  104 , which itself includes an impingement plate  106 , a drum separator  108 , a check valve  110 , a liquid outlet line  112 , and a dry gas outlet line  114 . 
     Liquid knockout drum  104  is shown to be a substantially cylindrical drum that is substantially rectangular in the cross section; however, in other embodiments the liquid knockout drum could be any other shape suitable to allow liquids and other fluids to collect below a dry gas outlet line. For example, a substantially spherical liquid knockout drum or surge tank that is substantially circular in the cross section could be used if it allowed for liquids and other fluids to collect below a dry gas outlet line. A liquid knockout drum or surge tank can be made of any suitable material or any suitable combination of materials known in the art such as steel, stainless steel, metal alloys, plastics, and composite materials. 
     In the embodiment of  FIG. 1 , the pressure in the liquid knockout drum  104  is about 66 atmospheres (atm) (about 950 pounds per square inch gauge (psig)) and the temperature is about 82° C. (about 180° F.). The liquid knockout drum  104  has a diameter of about 2 meters (m) and a height of about 3 m, and is located about 7 m upstream of the venturi meter  118 . In other embodiments, differently sized and shaped liquid knockout drums could be used to optimize liquid knockout responsive to system characteristics. In some embodiments, a liquid knockout drum is located between about 1 m and about 20 m upstream of a venturi meter. In other embodiments, a liquid knockout drum is located between about 5 m and about 10 m upstream of a venturi meter. In some embodiments, a liquid knockout drum is disposed between about 0.3 m (about 1 foot) and about 3 m (about 10 feet (ft)) above the ground. In other embodiments, a liquid knockout drum is disposed between about 0.60 m (about 2 ft) and about 1.22 m (about 4 ft) above the ground. 
     As shown, feedstream  102  enters liquid knockout drum  104  substantially perpendicularly to a side wall  116  of the liquid knockout drum  104 , and substantially in line with dry gas outlet line  114 . In other embodiments, a feedstream can enter a liquid knockout drum disposed at any suitable disposition or angle relative to the liquid knockout drum, and the feedstream need not enter the liquid knockout drum substantially in line with the dry gas outlet line or liquid outlet line. In some embodiments, the pressure and temperature within a liquid knockout drum are substantially equivalent to the pressure and temperature within a feedstream and a dry gas outlet line. 
     Impingement plate  106  is disposed within liquid knockout drum  104  and is disposed substantially perpendicular to, proximate to, and in front of inlet cavity  117  of feedstream  102 . Feedstream  102 , including wet gas in feedstream  102 , contacts impingement plate  106  within liquid knockout drum  104 . When the wet gas contacts impingement plate  106 , liquid fluids such as water, and potentially gas condensates, aggregate on impingement plate  106 , and the liquid fluids on impingement plate  106  run downwardly by gravity in the Y 1  direction toward drum separator  108  and check valve  110 . Impingement plate  106  can be disposed within liquid knockout drum  104  by any suitable means including any one of or any combination of, for example, welds, bolts, fasteners, screws, removable inserts, and suspension means. Without being bound by any theory or explanation, by using a metallic plate, which obstructs the feedstream comprising a liquid fluid, a sudden change in pressure occurs when the stream contacts the plate, and liquid is knocked out or separated from the gas. 
     Referring to  FIGS. 2A and 2B , certain example shapes are shown for impingement plates. Plate  200  is a substantially rectangular prism and has a length  202 , a width  204 , and thickness  206 . For use of plate  200  in the embodiment of  FIG. 1 , the length  202  and width  204  are both about 16 centimeters (cm) (6.30 inches (in)), such that a forward face  208  of plate  200  completely spans the inner diameter of feedstream  102  and inlet cavity  117 , which is about 15 cm (about 5.761 in), discussed further as follows. The thickness  206  of the plate  200  is about 1.27 cm (0.5 in) for use in the embodiment of  FIG. 1 . In other embodiments, the length, width, and thickness of an impingement plate can be adjusted and suitably fitted to a system responsive to any one of or any combination of the inner diameter of the feedstream, the pressure and temperature of the feedstream, the size, shape, and arrangement of the liquid knockout drum, the pressure and temperature of the liquid knockout drum, and the liquid content characteristics of the natural gas. 
     Plate  210  is a substantially cylindrical disc and has a diameter  212  and thickness  214 . For use of plate  210  in the embodiment of  FIG. 1 , the diameter  212  is about 16 cm (6.30 in), such that a forward face  216  of plate  210  completely spans the inner diameter of feedstream  102 , which is about 15 cm (about 5.761 in), discussed further as follows. The thickness  214  of the plate  210  is about 1.27 cm (0.5 in) for use in the embodiment of  FIG. 1 . In other embodiments, the diameter and thickness of an impingement plate can be adjusted and suitably fitted to a system responsive to any one of or any combination of the inner diameter of the feedstream, the pressure and temperature of the feedstream, the size, shape, and arrangement of the liquid knockout drum, the pressure and temperature of the liquid knockout drum, and the liquid content characteristics of the natural gas. 
     Referring again to  FIG. 1 , the impingement plate  106  is spaced at a distance S from the inlet cavity  117  of the feedstream  102 . In the embodiment of  FIG. 1 , impingement plate  106  is disposed about 0.5 m (about 1.6 ft) away from the inlet cavity  117 . In certain embodiments, one or more impingement plates are permanently disposed, such as, for example, by welding, within a liquid knockout drum; however, in other embodiments one or more impingement plates in a liquid knockout drum are interchangeable and removable, such as being slidable in channels and grooves within a liquid knockout drum. In the embodiment of  FIG. 1 , the impingement plate  106  is made substantially from steel, but in other embodiments any suitable material or combination of materials to cause liquid to aggregate on the impingement plate from the wet gas stream can be used. 
     In some embodiments any one of or any combination of the size, shape, amount, disposition, material composition, permanence, temperature, or interchangeability of one or more impingement plates within a liquid knockout drum are responsive to any one of or any combination of the inner diameter of the feedstream, the pressure and temperature of the feedstream, the size, shape, and arrangement of the liquid knockout drum, the pressure and temperature of the liquid knockout drum, and the liquid content characteristics of the natural gas. 
     In some embodiments, all or portions of an impingement plate are solid or hollow. In some embodiments, the forward face of an impingement plate facing the inlet cavity of the wet gas feedstream is substantially solid and flat; however, in other embodiments the forward face of an impingement plate facing a wet gas feedstream can have holes, cavities, or pores, optionally to increase surface area for liquid aggregation and dropout into the liquid knockout drum. In some embodiments, an impingement plate can have through-channels for potential condensates and liquid dropout to travel by gravity downwardly to a check valve substantially through the impingement plate. In some embodiments, the temperature of the impingement plate is controlled either by heating or cooling to increase the amount of liquid knocked out of the gas stream. 
     In the embodiment shown in  FIG. 1 , there is one impingement plate  106 . However, in other embodiments, more or fewer impingement plates could be placed within a liquid knockout drum. More or fewer liquid knockout drums could be placed in any arrangement and position to optimize liquid fluid removal from the wet gas. For instance, a series of impingement plates can be placed throughout a liquid knockout drum to optimize liquid and potential condensate collection near a check valve for the fluid to be drained before a venturi meter. In other embodiments, the liquid knockout drum can collect liquid fluids, with one or more impingement plates placed in a gas inlet or gas outlet line, and not within the liquid knockout drum itself. 
     Water and other liquids that aggregate on impingement plate  106  or otherwise drop out of the wet gas in liquid knockout drum  104  fall by way of gravity in the Y 1  direction toward drum separator  108 . As shown, drum separator  108  slants downwardly in the Y 1  direction from the side wall  116  toward the check valve  110 . The drum separator  108  is a thin, water-proof steel sheet in the embodiment of  FIG. 1 . Drum separator  108  separates an upper portion  107  of liquid knockout drum  104  from a lower portion  109 , and liquid fluid flows from the upper portion  107  to the lower portion  109  by way of check valve  110  when check valve  110  is in an open state. In other embodiments, a drum separator can be any thin layer that fluidly separates an upper portion of a liquid knockout drum from a lower portion of the liquid knockout drum. 
     Check valve  110  allows for the one-way flow of liquid fluid downwardly in the Y 1  direction from the liquid knockout drum  104  to the liquid outlet line  112 . Fluid, such as gas and liquid, will not flow upwardly in the Y 2  direction through the check valve  110 . In the embodiment of  FIG. 1 , the check valve  110  opens responsive to the liquid level accumulated above the check valve  110 . Check valve  110  opens when liquid accumulated above check valve  110  reaches level L 1 , and the check valve  110  closes when the liquid is reduced to level L 2  by flowing through check valve  110  to lower portion  109 . 
     The liquid levels L 1  and L 2  can be detected or measured by any means known in the art for detecting liquid levels including sonar, for example. In addition, check valve  110  can be calibrated to open when a certain mass of liquid rests above check valve  110 , and can similarly be calibrated to close when a lesser mass of liquid rests above check valve  110 . When the check valve  110  is open, fluid flows downwardly by gravity in the Y 1  direction toward liquid outlet line  112  and is forced through liquid outlet line  112  by the pressure from liquid knockout drum pressure line  122  when liquid knockout valve  128  is open, discussed further as follows. Liquid knockout valve  128  and liquid outlet valve  130  are optional and neither is required, as gas can be allowed to passively flow though liquid knockout drum pressure line  122  and liquid outlet line  112  at all times. 
     In some embodiments, a check valve is set to open when a predetermined amount of liquid fluid is accumulated at the check valve in a liquid knockout drum. In other embodiments, the check valve is set to open at predetermined time intervals when a gas feedstream is flowing. In other embodiments, a user determines when to open the check valve based on the amount of liquid fluid collected at the check valve, and a user can do so through any one of or any combination of a remote connection, a wireless connection, and a wired connection. In some embodiments, the pressure above a check valve in the Y 2  direction is substantially the same as the pressure below the check valve in the Y 1  direction. In other embodiments, the pressure above a check valve in the Y 2  direction is substantially different than the pressure below the check valve in the Y 1  direction. In some embodiments, the pressure differential between a portion of a liquid knockout drum above a check valve and a portion of a liquid knockout drum below a check valve is about ±15 psig. 
     Dry gas outlet line  114  proceeds to and is in fluid communication with venturi meter  118 . Any commercially-available venturi meter is envisioned for use in the systems and methods of the present disclosure. For example, venturi meters sold by ABB Ltd., headquartered in Zurich, Switzerland, are envisioned for use with the systems and methods of the present disclosure. One such meter has an inner pipe diameter of about 103.7 millimeters (mm) and a constricted throat diameter of about 73.2 mm. 
     As a fluid, such as natural gas, flows from dry gas outlet line  114  with diameter D 1  through venturi meter  118  with a constricted diameter D 2 , the fluid&#39;s velocity must increase, and the static pressure decreases. By measuring the change in pressure, the flow rate of a fluid can be determined. Dry gas outlet line  114  comprises dry gas from which water, and other liquids, have been removed. This increases the accuracy of measurement of venturi meter  118 , as only one fluid phase (gas) is passing through the meter rather than two fluid phases (gas and liquid). Importantly, embodiments of the present disclosure contemplate applying systems and methods to existing venturi meters in existing gas pipelines, and additional meters, such as gas turbine flow meters and water cut meters, are not required. 
     In addition to single-phase fluid flow meters that use a constricted diameter to measure fluid flow by a change in differential pressure of the flowing fluid, such as venturi meters, the systems and methods of the present disclosure are contemplated to increase the accuracy of any flow measurement device that is primarily designed for single-phase flow measurement by removing liquid from a gas stream, provided that the device is in the proximity of a pressure choke valve (pressure chock) to provide higher pressure for re-introducing the separated fluid downstream of the pressure choke valve. 
     Post-venturi pipe segment  120 , in which dry gas expands after passing through venturi meter  118 , provides pressure to liquid knockout drum pressure line  122 . Liquid knockout drum pressure line  122  pressurizes liquids in the liquid knockout drum  104 , which have passed through check valve  110 . The pressure from liquid knockout drum pressure line  122  drives liquids through the liquid outlet line  112  to the manifold line  124 . Dry gas from post-venturi pipe segment  120  is recombined with liquid fluid in manifold line  124  after passing through pressure choke  126 . In this way, the venturi meter  118  measures only dry gas, but there is no additional line needed to carry away liquid fluids, as they are recombined in the manifold line  124 . 
     Pressure choke  126 , liquid knockout valve  128 , and liquid outlet valve  130  control and regulate the gas flow in system  100 . Any one of or any combination of pressure choke  126 , liquid knockout valve  128 , and liquid outlet valve  130  can be manually controlled (opened and closed) by a user or operator and can be automated and controlled by a distributed control system (DCS) (not shown) used in natural gas pipeline systems. For example, in system  100 , if liquid fluid were flowing through check valve  110  (in other words check valve  110  were open), then liquid knockout valve  128  can either be manually opened by a user or automatically set to open, responsive to opening of check valve  110 , to allow gas flow from liquid knockout drum pressure line  122  to drive the liquid through liquid outlet line  112 . In this case, liquid outlet valve  130  would also need to be open to allow the liquid and gas to flow to the manifold line  124 . 
     Depending on the gas flow needed from liquid knockout drum pressure line  122  to drive the liquid through liquid outlet line  112 , pressure choke  126  and liquid knockout valve  128  could be partially or fully open (either manually or automatically responsive to the amount of liquid that needs to be driven out of the liquid knockout drum  104  through liquid outlet line  112 ) to increase the gas flow in liquid knockout drum pressure line  122 . 
     As noted previously, the pressure in the liquid knockout drum  104  is about 950 psig and the temperature is about 180° F., in some embodiments. The pressure downstream of the pressure choke  126 , for example in the manifold line  124 , is about 59 atm to about 62 atm (about 850 psig to about 900 psig), and the temperature is in the range of about 66° C. to about 71° C. (about 150° F. to about 160° F.). For example, in some embodiments of operation of system  100 , a pressure P 1  at feedstream  102  minus a pressure P 2  at the dry gas outlet line  114  is greater than a pressure P 4  in lower portion  109  of liquid knockout drum  104 ; a pressure P 3  at post-venturi pipe segment  120  is greater than pressure P 4  in lower portion  109  of liquid knockout drum  104 ; and pressure P 4  in lower portion  109  of liquid knockout drum  104  is greater than a pressure P 5  in manifold line  124 . In some embodiments, differential pressure across a pre-existing gas pipeline pressure choke, such as for example pressure choke  126 , allows the efficient operation of systems and methods of the present disclosure. 
     In the system  100 , if the check valve  110  were closed, the system could be programmed to automatically close liquid knockout valve  128  and liquid outlet valve  130  such that gas flow proceeded only through pressure choke  126  to the manifold line  124 . In some embodiments, system  100  can include one or more optional liquid flow meters  132  on liquid outlet line  112 . 
     In the embodiment of  FIG. 1 , the outer diameter of the feedstream  102 , the dry gas outlet line  114 , and the manifold line  124  is about 17 cm (about 6.625 in) and the inner diameter, D 1 , of the feedstream  102 , the dry gas outlet line  114 , and the manifold line  124  is about 15 cm (about 5.761 in). In the embodiment shown, feedstream  102 , dry gas outlet line  114 , and manifold line  124  are made substantially from steel. In other embodiments, other size pipes made from any other pipe material known in the art, such as plastic, can be used with the systems and methods of the present disclosure. 
     Still referring to  FIG. 1 , the outer diameter of the liquid knockout drum pressure line  122  and the liquid outlet line  112  is about 9 cm (about 3.5 in) and the inner diameter of the liquid knockout drum pressure line  122  and the liquid outlet line  112  is about 7 cm (about 2.624 in). In the embodiment shown, liquid knockout drum pressure line  122  and the liquid outlet line  112  are made substantially from steel. In other embodiments, other size pipes made from any other pipe material known in the art, such as plastic, can be used with the systems and methods of the present disclosure. 
     The venturi meter  118  is located upstream, or ahead of, the pressure choke  126 . Using the pressure choke  126 , line pressure in post-venturi pipe segment  120  can be maintained to be greater than the line pressure in manifold line  124 . This pressure differential helps to pressurize the separated liquids in lower portion  109  of liquid knockout drum  104  to reintroduce them into the lower pressure portion downstream of the pressure choke  126  into manifold line  124 . The differential pressure across pressure choke  126  can be different for each well and can range from about 10 psig to about 1,000 psig. Valves  128  and  130  help further to fine tune the pressures within the system. 
     Referring now to  FIG. 3 , a flow chart is provided for one exemplary method of liquid knockout for a wet gas well using the embodiment of the system shown in  FIG. 1  and described previously. Any of the steps described can be carried out by a user or operator, or can be automated and carried out by an automated distributed control system using any one of or any combination of wired and wireless connections to components. First, at step  300 , feedstream  102  comprising wet gas is activated to flow in a natural gas pipeline system toward the liquid knockout system  100  comprising the liquid knockout drum  104  and the impingement plate  106 . The liquid knockout drum  104  includes at least one impingement plate  106  for removal of water and other liquid fluids from the wet gas feedstream  102 . 
     At step  302 , pressure choke  126  is open, and liquid knockout valve  128  and liquid outlet valve  130  are closed. In this step, all of the dry gas flows to the manifold line  124  by way of the post-venturi pipe segment  120 , as liquids fall out of the wet gas in liquid knockout drum  104  and accumulate on drum separator  108  around check valve  110 . At step  304 , liquid fluids in the liquid knockout drum  104  have reached level L 1 , and the check valve  110  is opened to allow liquid to flow to liquid outlet line  112 , until the liquid level in liquid knockout drum  104  has reached level L 2 . At step  306 , liquid knockout valve  128  and liquid outlet valve  130  are opened such that gas in liquid knockout drum pressure line  122  drives the liquid through liquid outlet line  112  to manifold line  124 . 
     At step  308 , the pressure choke  126  is partially constricted to redirect more gas through liquid knockout drum pressure line  122 . At step  310 , when the liquid level returns to level L 2  from level L 1 , the check valve  110  is closed. At step  312 , the pressure choke  126  is fully unconstricted. At step  314 , the liquid knockout valve  128  and liquid outlet valve  130  are closed. After step  314 , the process described from step  304  to step  314  will continue, until the system  100  is deactivated at step  316 , for instance when the feedstream  102  is deactivated. 
     In the various embodiments of the disclosure described, a person having ordinary skill in the art will recognize that various types of memory are readable by a computer, such as the memory described in reference to the various computers and servers, e.g., computer, computer server, web server, or other computers with embodiments of the present disclosure. 
     The singular forms “a,” “an,” and “the” include plural referents, unless the context clearly dictates otherwise. 
     In the drawings and specification, there have been disclosed embodiments of systems and methods for accurate measurement of gas from wet gas wells of the present disclosure, and although specific terms are employed, the terms are used in a descriptive sense only and not for purposes of limitation. The embodiments of the present disclosure have been described in considerable detail with specific reference to these illustrated embodiments. It will be apparent, however, that various modifications and changes can be made within the spirit and scope of the disclosure as described in the foregoing specification, and such modifications and changes are to be considered equivalents and part of this disclosure.