Abstract:
A self contained, trailer mounted condensation collection system for an oil and gas well. The system has a condenser for cooling and condensing those oil well gases that can be condensed and a separator for separating the condensed portion from the non-condensable portion of the gas stream so that the condensed gases can be recovered as liquid hydrocarbons. The system is powered by the gas pressure from the well and operates without any outside utilities so that it can be used at new well sites where infrastructure has not been built to support the well.

Description:
BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     The present invention is a self contained, trailer mounted system with condenser for cooling and condensing those oil well gases that can be condensed and with a separator for separating the condensed portion from the non-condensable portion of the gas stream so that they can be recovered as liquid hydrocarbons. The system is powered by the gas pressure from the well and operates without any outside utilities so that it can be used at new well sites where infrastructure has not been built to support the well. 
     2. Description of the Related Art 
     In today&#39;s era of oil and gas well drilling, often wells will be drilled in remote locations where there are no utilities and no gas gathering pipelines. In shale areas such as the Baaken, Marcellus, Utica, and Eagle Ford areas, the wells are known to produce significant quantities of very light gravity crude oil, condensate (also known as natural gas liquids or NGLs) and natural gas in abundance. Since the completion technologies are relatively new, and these fields are quite large in geographical area, they lack the infrastructure necessary to bring all of the hydrocarbons into the commercial stream. At these wells, it has not been feasible to condense those hydrocarbons that exit the wellhead in gaseous state that might otherwise have been condensed to a liquid state and pumped to an oil tank. Therefore, large quantities of valuable hydrocarbon liquid rich natural gas are being released into the atmosphere, either directly or through venting or flaring. Often the condensable hydrocarbons are being burned with the non-condensable gases in flares at the wellhead, resulting in the loss of a large amount of recoverable hydrocarbons. With the high price of petroleum, this loss can add up to a considerable loss of revenue. 
     Also, the state and locate EPA offices in North Dakota, Pennsylvania, Ohio and Texas are now requiring that all wellhead gas be conditioned to remove as much of the valuable natural gas liquids as possible. This adds to the need for a new technology to remove the natural gas liquids prior to venting or flaring. 
     At the majority of these new wells, all gas and valuable natural gas liquids are being flared and completely destroyed by burning. The present system condenses and captures a portion of the valuable hydrocarbon liquids before they are sent to the flare, increasing the amount of hydrocarbon liquids entering the economic stream, and minimizing the waste and pollution associated with burning these valuable and much-needed products. 
     Also, burning hydrocarbon liquids generates considerable air pollution. This sort of air pollution was targeted in the Clean Air Act of 1970 as a known carcinogen. The present invention not only returns valuable hydrocarbons to the economic stream, it also generates a “green” benefit by reducing smog and the health hazards associated with it. 
     The present invention addresses this problem by providing a trailer mounted condensate collection system that is capable of using the pressure from the well to operate the system without the need for outside utilities. The system is a trailer mounted condensate optimization system designed to capture otherwise flared or lost hydrocarbon liquids. The system includes a trailer mounted condenser and a trailer mounted separator. It is specifically designed to be rugged enough for transportation to any well site on what are typically rough lease roads. 
     The present system treats the gases flowing from the well to condense, separate, and recover those gases that are capable of being condensed to a liquid from those gases that are non-condensable. Once on site, the system is connected to the well&#39;s flow line on the inlet end of the system and to the oil storage tank. The system is also connected on its outlet end to a flare, a vent stack or a gas pipeline when a gas pipeline is available. 
     The system uses pressure from the well to operate a fan that blows ambient air across a heat exchanger where those hydrocarbons from the wellhead that can be condensed will cool sufficiently to condense to a liquid state. 
     From the heat exchanger, the mixed gaseous and liquid effluent then flows through a separator where the effluent is initially used to heat the separator and then the effluent is introduced into the separator where the liquid portion is separated from the gaseous portion. The separated liquid portion is discharged to an oil storage tank where the liquids that flowed from the well are stored, and the separated gaseous portion is discharged to a flare to be burned or to a gas pipeline when one is available. 
     As any oil and gas producing area matures, the infrastructure grows to accommodate the need to gather, refine, and process the hydrocarbons to the greatest benefits of the owners. As this infrastructure is put in place the need for wellhead gas liquids condensation systems will shift to areas still outside the influence of infrastructure systems. Wells still remote to new gas gathering pipeline systems and gas plants will still need mobile condensation collection systems like the present invention, at least until the entire field is blanketed by the necessary pipeline networks. In the known shale oil areas of the United States, these plays are so large it may be a century or more before the infrastructure development is truly complete. That assures the present invention a full and fertile future for many decades ahead. 
     With over 160 drilling rigs currently running in the Baaken within a 50 mile radius of Williston, N. Dak., and with the price of crude oil still rising steadily, the opportunities for the present system continue to grow. And the Baaken is just one basin and one area. The same conditions exist in other shale reserves. 
     Rigs are completing wells at a rate of about one per month from spud to completion of fracturing. Therefore, in the Baaken alone, nearly 2000 new wells were completed and brought on line in 2012. The extrapolation of this into a nationwide new shale oil and gas well development makes it clear that there is a great need for the present invention. 
     SUMMARY OF THE INVENTION 
     The present invention is a trailer mounted condensate collection system that is capable of using the pressure from the well to operate the system without the need for outside utilities. The system is a trailer mounted condensate optimization system designed to capture otherwise flared or lost hydrocarbon liquids. The system includes a trailer mounted condenser and a trailer mounted separator. It is specifically designed to be rugged enough for transportation to any well site on what are typically rough lease roads. 
     The present system treats the gases flowing from the well to condense, separate, and recover those gases that are capable of being condensed to a liquid from those gases that are non-condensable. Once on site, the system is connected to the well&#39;s flow line on the inlet end of the system and to the oil storage tank. The system is also connected on its outlet end to a flare, a vent stack or a gas pipeline when a gas pipeline is available. 
     As the gaseous stream from the well enters the system, the pressure is first reduced through a gas operated back pressure regulator valve to control the inlet pressure to the system. The system uses a stream of gas from the well to operate a gas powered fan that blows ambient air across an air heat exchanger where those hydrocarbons from the wellhead that can be condensed will cool sufficiently to condense to a liquid state. Once the pressure of the gaseous stream has been reduced, the gaseous stream then enters the air heat exchanger where the inlet gas is cooled to a temperature within 5-10 degrees from ambient air temperature. The air exchanger is a specially designed industrial horizontal in-fan with an under-mounted large diameter multi-blade fan below several horizontal passes of small diameter high pressure finned process gas/fluid containing tubes. The fan driven cooler moves ambient air across the various layers of finned tubes, cooling the tubes and thus the gases/liquids within the tubes, causing the once gaseous stream that entered the heat exchanger to condense to liquid and forming a mixture of gas and liquid within the tubes. This typically produces a temperature reduction of from 50-100 degrees Fahrenheit, depending on ambient conditions. The air exchanger is unique to this application in that its fan is driven by an air powered (or in this case gas powered) motor, eliminating the need for a conventional electric motor, since more often than not, electricity is not available on the target new well sites. 
     The cooled liquids and gases exit the exchanger and then enter into a horizontal chiller-separator mounted on the trailer. This specially designed separator has a finned process cooling coil in the lower liquid phase portion of the separator tank. The Jules Thompson cooling effect of the upstream components creates a rain-like environment inside the separator allowing otherwise lost hydrocarbon fractions to condense out of the gas phase into the liquid phase within the separator tank. 
     The finned process cooling coil in the bottom of the separator maintains the cool liquid temperature, stabilizing the liquid temperature to prevent re-evaporation. The result is a dramatic increase in recoverable hydrocarbon liquids. 
     As the stable hydrocarbon liquid volume grows inside the separator, a gas operated liquid level controller senses the liquid level and sends a signal to a special freeze-proof oil valve to open, allowing the recovered liquid oil to move on to storage. The much enhanced volume of recovered hydrocarbon liquid then flows through a long-life battery powered and highly accurate turbine flow meter that counts each barrel of oil in increments of 1/1000ths of a barrel and electronically totalizes the flow on a continuously readable LCD display. The oil then exits the trailer mounted system and the separated liquid oil portion is discharged to an oil storage tank where the liquids that flowed from the well are stored and is ready for sale as crude oil. 
     The remaining well stream or separated gaseous portion is now lean gas, free of condensable hydrocarbons. It is released or discharged from the trailer mounted system through a second gas operated back pressure valve from which it flows on to the lease flare stack to be burned, or alternately, to a gas pipeline when one is available. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a diagram showing the component parts of the present invention in relationship to an oil well and in relationship to a gas flare, an oil tank and a waste water tank that are located at the well site. 
         FIG. 2  is an enlarged view of the area within dashed line  10  of  FIG. 1 . 
     
    
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT 
     Referring now to  FIGS. 1 and 2 , there is illustrated a trailer mounted condensate collection system  10  constructed in accordance with a preferred embodiment of the present invention.  FIG. 1  is a diagram of the component parts of the system  10  that are mounted on a trailer  11 , with the components of the system  10  shown within the dashed line enclosure associated with numeral  10 .  FIG. 1  shows the trailer mounted system  10  in relationship to an oil and gas producing well  12  and in relationship to a gas flare  14 , an oil storage tank  16  and a waste water tank  18  that are located at the well site. 
     The trailer mounted condensate collection system  10  is capable of using the gas pressure from the well  12  to operate the system  10  without the need for outside utilities. The trailer mounted condensate optimization system  10  is designed to capture otherwise flared or lost hydrocarbon liquids that would be exiting from the well  12  in the gas stream. The system  10  includes a trailer  11  on which is mounted a condenser  20  and a separator  22  and associated valves and equipment as will be described hereafter. It is specifically designed to be rugged enough for transportation to any well site over rough lease roads. 
     Referring now to the drawing, the system  10  will be described. The present system  10  treats the gases flowing from the well  12  to condense those gases that are capable of being condensed to a liquid, to separate the condensed liquids from those gases that are not condensed, and to recover those condensed liquids. Once on site, the system  10  is connected to the well&#39;s gas flow line  24  on the inlet end  26  of the system  10 . On the outlet end  26  of the system  10 , connections are made to an oil storage tank  16 , to a waste water tank  18  and to either a flare  14 , a vent stack (not illustrated) or a gas pipeline (also not illustrated), if a gas pipeline is available at the well site. 
     As the gaseous stream from the well  12  enters the system  10 , the pressure is first reduced through a gas operated inlet back pressure regulator valve  30  to control the inlet pressure to the system  10 . The system  10  uses a stream of gas from the well  12  to operate a pneumatic powered fan  32  that blows ambient air across an air heat exchanger  34  of the condenser  20 . The air heat exchanger  34  is where those gaseous hydrocarbons from the well  12  that can be condensed will be cooled sufficiently to condense to a liquid state. 
     Once the pressure of the gaseous stream has been reduced, the gaseous stream then enters the air heat exchanger  34  of the condenser  20  where the inlet gas is cooled to a temperature that is within approximately 5-10 degrees from ambient air temperature. The condenser  20  is a specially designed industrial horizontal fin-fan air exchanger  34  with an under-mounted large diameter multi-blade fan  32  located below several horizontal passes of small diameter high pressure finned process gas containing heat exchanger tubes  36  containing the gaseous stream from the well  12 . The fan driven cooler or condenser  20  moves ambient air across the various layers of finned tubes  36 , cooling the tubes  36  and thus the gas within the tubes  36 , causing a portion of the gaseous stream that entered the heat exchanger  34  to condense to liquid and forming a mixture of gas and liquid within the tubes  36 . This typically produces a temperature reduction of the gas and liquid stream from 50-100 degrees Fahrenheit, depending on ambient conditions. 
     The air heat exchanger  34  is unique to this application in that its fan  32  is driven by an air powered fan motor  38 . In this case the gas that powers the motor  38  is not air, but is instead the pressurized gas from the well  12 . Use of this type of fan motor eliminates the need for a conventional electric motor, since more often than not, electricity is not available on the target new well sites. 
     The cooled mixture of liquids and gases exits the exchanger  34  and then enters into a horizontal chiller-separator  22  that is also mounted on the trailer  11  along with the air exchanger  34 . This specially designed separator  22  has a finned process cooling coil  40  contained in the lower liquid phase portion of the separator  22 . The Jules Thompson cooling effect of the upstream components creates a rain-like environment inside the separator  22  allowing otherwise lost hydrocarbon fractions to condense out of the gas phase into the liquid phase within the separator  22 . 
     The finned process cooling coil  40  in the bottom of the separator  22  maintains the cool liquid temperature, stabilizing the liquid temperature to prevent re-evaporation. The result is a dramatic increase in recoverable hydrocarbon liquids. 
     The temperature within the separator  22  is monitored by a temperature controller  42  that opens a separate bypass control valve  44  to bypass the system  10  with the well&#39;s gas stream if the temperature within the separator  22  approaches temperatures low enough that the entrained water that was contained in the gas and liquid stream and is separated from the hydrocarbons in the separator  22  might be in danger of freezing within the separator  22  before it can be discharged to the waste water tank  18 . 
     The separator  22  is provided with a gas operated water level controller  46  that senses the level of water within the separator  22  and sends a signal to activate a freeze-proof water dump valve  48  to open, allowing water to be discharged from the bottom of the separator  22  to maintain the proper water level in the separator  22 . The discharged water flows from the system  10  and into the waste water tank  18 . 
     As the stable hydrocarbon liquid volume grows inside the separator  22 , a gas operated liquid level controller  50  senses the liquid level and sends a signal to a special freeze-proof oil valve  52  to open, allowing the recovered liquid oil to exit the separator  22 . The much enhanced volume of recovered hydrocarbon liquid then flows through a long-life battery powered and highly accurate turbine flow meter  54  that counts each barrel of oil passing through the meter  54  in increments of 1/1000ths of a barrel and electronically totalizes the flow on a continuously readable LCD display  56 . The separated liquid oil portion then exits the trailer mounted system  10  and flows to the oil storage tank  16  where the liquid hydrocarbons that initially flowed from the well  12  are stored and ready for sale as crude oil. 
     Referring back to the separator  22 , a drip trap  58  is provided in-line on the gas line  60  that supplies control gas to the separator&#39;s temperature controller  42 , to the oil liquid level controller  50  and to the water level controller  46  to protect these instruments by preventing liquids from reaching them in the control gas. 
     The remaining well stream or separated gaseous portion is now lean gas that is free of condensable hydrocarbons. It is released or discharged from the trailer mounted system  10  through a second gas operated back pressure valve  62  from which it flows on to the lease flare  14  to be burned, or alternately, to a gas pipeline when one is available at the well site.  FIG. 1  shows the gaseous portion being conducted to a gas flare  14 . 
     While the invention has been described with a certain degree of particularity, it is manifest that many changes may be made in the details of construction and the arrangement of components without departing from the spirit and scope of this disclosure. It is understood that the invention is not limited to the embodiments set forth herein for the purposes of exemplification, but is to be limited only by the scope of the attached claim or claims, including the full range of equivalency to which each element thereof is entitled.