초록 ▼

Systems and methods for cleaning the interior surfaces of tubular members are provided. A flexible conduit having a nozzle disposed on an end can be disposed within the bore of a tubular to be cleaned. The nozzle can have an internal 5-15 degree tapered section with a length-to-diameter ratio of gre

Systems and methods for cleaning the interior surfaces of tubular members are provided. A flexible conduit having a nozzle disposed on an end can be disposed within the bore of a tubular to be cleaned. The nozzle can have an internal 5-15 degree tapered section with a length-to-diameter ratio of greater than about 2:1. The nozzle can have an outer diameter that is about 80% to 99% of the inner diameter of the tubular. A fluid suspension containing air and solid carbon dioxide can be passed through the nozzle, impinging the surrounding inner surface of the surrounding tubular as the nozzle is disposed within the tubular. The solid carbon dioxide and compressed air suspension can have a solids concentration of from about 0.1% to 10.0% solids. The solids delivery rate through the nozzle can range from about 0.5 lbs/minute to about 5 pounds/minute. The flow of the suspension through the nozzle can be controlled using a remote device.

대표청구항 ▼

1. A method for cleaning one or more tubulars, comprising: mixing a plurality of carbon dioxide solids in a compressed air stream to form a fluid suspension containing from about 0.75 wt % to about 7.5 wt % carbon dioxide solids, wherein the carbon dioxide solids are in the form of rice-shaped elong

1. A method for cleaning one or more tubulars, comprising: mixing a plurality of carbon dioxide solids in a compressed air stream to form a fluid suspension containing from about 0.75 wt % to about 7.5 wt % carbon dioxide solids, wherein the carbon dioxide solids are in the form of rice-shaped elongated prills having an outside diameter from about 0.093 inches to about 0.125 inches and a bulk density from about 30 lbs/ft3 to about 60 lbs/ft3, and wherein a pressure of the compressed air is from about 100 psig to about 300 psig;flowing the fluid suspension through a flexible conduit having a nozzle disposed at an end thereof, wherein the nozzle is coupled to the flexible conduit with a connector, wherein the connector is integral with the nozzle and has threads disposed on an outer surface thereof, wherein the flexible conduit, the connector, and the nozzle all remain open and unobstructed when the fluid suspension is flowing therethrough, and wherein a feed rate of the carbon dioxide solids is from about 0.5 lb/min to about 10 lb/min;locating the nozzle within a tubular, wherein an outer diameter of the nozzle is about 95% to about 99.9% of an inner diameter of the tubular;cleaning an inner surface of the tubular by impinging the carbon dioxide solids against the inner surface of the tubular, wherein the carbon dioxide solids form a conical pattern after exiting the nozzle, and wherein a minimum of 70 wt % of the carbon dioxide solids are distributed about the perimeter of the conical pattern; andremotely controlling the flow of the fluid suspension through the nozzle to limit a temperature drop of the surface to about 20° F. or less, wherein: the nozzle has a bore defined by a single tapered inner surface such that the bore has a frustoconical shape extending from a first end of the nozzle to a second end of the nozzle,a diameter of the bore at the second end of the nozzle is about 2.4 times a diameter of the bore at the first end of the nozzle,an angle between the single tapered inner surface and a longitudinal centerline of the nozzle is from about 7° to about 12°,the nozzle has a length to outer diameter ratio from about 2:1 to about 10:1, andthe first end of the nozzle is adjacent the end of the flexible conduit. 2. The method of claim 1, wherein the temperature drop of the surface is limited to about 10° F. or less, wherein the angle between the single tapered inner surface and the longitudinal centerline of the nozzle is from about 7° to about 10°, wherein the nozzle has a length to an outer diameter ratio from about 5:1 to about 7:1. 3. The method of claim 1, wherein the outer diameter of the nozzle is from about 0.001 inches to about 0.01 inches less than the inner diameter of the tubular. 4. The method of claim 1, wherein the inner diameter of the tubular is about 0.25 inches to about 6 inches. 5. The method of claim 1, wherein the flow of the fluid suspension through the nozzle is remotely controlled to limit the temperature drop of the surface to about 10° F. or less. 6. The method of claim 1, further comprising moving the nozzle within the tubular at a speed of about 1 inch per minute to about 100 inches per minute. 7. A method for cleaning one or more tubulars, comprising: mixing a plurality of carbon dioxide solids in a compressed air stream to form a fluid suspension containing from about 0.75 wt % to about 7.5 wt % carbon dioxide solids, wherein the carbon dioxide solids are in the form of rice-shaped elongated prills having an outside diameter from about 0.093 inches to about 0.125 inches and a bulk density from about 30 lbs/ft3 to about 60 lbs/ft3, and wherein a pressure of the compressed air is from about 100 psig to about 300 psig;flowing the fluid suspension through a flexible conduit having a nozzle disposed at an end thereof, wherein the nozzle is coupled to the flexible conduit with a connector, wherein the connector is integral with the nozzle and has threads disposed on an outer surface thereof, wherein the flexible conduit, the connector, and the nozzle all remain open and unobstructed when the fluid suspension is flowing therethrough, and wherein a feed rate of the carbon dioxide solids is from about 0.5 lb/min to about 10 lb/min;locating the nozzle within a tubular, wherein an outer diameter of the nozzle is about 95% to about 99.9% of an inner diameter of the tubular;cleaning an inner surface of the tubular by impinging the carbon dioxide solids against the inner surface of the tubular, wherein the carbon dioxide solids form a conical pattern after exiting the nozzle, and wherein a minimum of 90 wt % of the carbon dioxide solids are distributed about the perimeter of the conical pattern; andremotely controlling the flow of the fluid suspension through the nozzle to limit a temperature drop of the surface to about 10° F. or less, wherein: the nozzle has a bore defined by a single tapered inner surface such that the bore has a frustoconical shape extending from a first end of the nozzle to a second end of the nozzle,a diameter of the bore at the second end of the nozzle is about 2.4 times a diameter of the bore at the first end of the nozzle,an angle between the single tapered inner surface and a longitudinal centerline of the nozzle is from about 7° to about 10°,the nozzle has a length to outer diameter ratio from about 5:1 to about 7:1, andthe first end of the nozzle is adjacent the end of the flexible conduit. 8. The method of claim 7, wherein the outer diameter of the nozzle is from about 0.001 inches to about 0.01 inches less than the inner diameter of the tubular. 9. The method of claim 7, wherein the inner diameter of the tubular is about 0.25 inches to about 6 inches. 10. The method of claim 7, further comprising moving the nozzle within the tubular at a speed of about 1 inch per minute to about 100 inches per minute. 11. A method for cleaning one or more tubulars, comprising: mixing a plurality of carbon dioxide solids in a compressed air stream to form a fluid suspension containing from about 0.75 wt % to about 7.5 wt % carbon dioxide solids, wherein the carbon dioxide solids are in the form of rice-shaped elongated prills having an outside diameter from about 0.093 inches to about 0.125 inches and a bulk density from about 30 lbs/ft3 to about 60 lbs/ft3, and wherein a pressure of the compressed air is from about 100 psig to about 300 psig;flowing the fluid suspension through a flexible conduit having a nozzle disposed at an end thereof, wherein the nozzle is coupled to the flexible conduit with a connector, wherein the connector is integral with the nozzle and has threads disposed on an outer surface thereof, wherein the flexible conduit, the connector, and the nozzle all remain open and unobstructed when the fluid suspension is flowing therethrough, and wherein a feed rate of the carbon dioxide solids is from about 0.5 lb/min to about 5 lb/min;locating the nozzle within a tubular, wherein an outer diameter of the nozzle is about 99% to about 99.9% of an inner diameter of the tubular, and wherein the outer diameter of the nozzle is from about 0.001 inches to about 0.01 inches less than the inner diameter of the tubular;cleaning an inner surface of the tubular by impinging the carbon dioxide solids against the inner surface of the tubular, wherein the carbon dioxide solids form a conical pattern after exiting the nozzle, and wherein a minimum of 90 wt % of the carbon dioxide solids are distributed about the perimeter of the conical pattern, wherein cleaning the inner surface of the tubular further comprises moving the flexible conduit and nozzle coaxially along a longitudinal axis of the tubular while maintaining an outer surface of the nozzle parallel to the inner surface of the tubular; andremotely controlling the flow of the fluid suspension through the nozzle to limit a temperature drop of the surface to about 10° F. or less, wherein: the nozzle has a bore defined by a single tapered inner surface such that the bore has a frustoconical shape extending from a first end of the nozzle to a second end of the nozzle,a diameter of the bore at the second end of the nozzle is about 2.4 times a diameter of the bore at the first end of the nozzle,an angle between the single tapered inner surface and a longitudinal centerline of the nozzle is from about 7° to about 10°,the nozzle has a length to outer diameter ratio from about 5:1 to about 7:1, andthe first end of the nozzle is adjacent the end of the flexible conduit. 12. The method of claim 11, wherein the inner diameter of the tubular is about 0.25 inches to about 6 inches. 13. The method of claim 11, wherein the flexible conduit and nozzle are moved at a speed of about 1 inch per minute to about 100 inches per minute along the longitudinal axis of the tubular.