In situ foam generation apparatus for on-site, on-demand, economical production of foaming solvents

Abstract

An in-situ foam generation apparatus includes a dissolution chamber that houses a polymer stick cavity or canister, a mixing chamber that houses a static mixer, and a foaming chamber that houses a mechanical agitator in fluid communication with a compressed air inlet. The chambers are in fluid communication with one another by way of a respective chamber inlet and outlet, with the mixing chamber being located between the dissolution and foaming chambers. A pressure regulator can be used to control the incoming aqueous solution pressure to the dissolution chamber. A nozzle exhaust is in fluid communication with the outlet of the foaming chamber. One or more polymer sticks that include one or more cleaning agent can be loaded into the cavity or canister of the dissolution chamber. An end consistency of the polymer stick can be in a range of partially solidified to fully solidified.

Claims

1. A wand for continuously delivering a surface activation (cleaning) agent on-demand as foam, the wand comprising: a water inlet configured for connection to a pressurized source of water; a mixing chamber located downstream of the water inlet; an air inlet configured for connection to a pressurized source of air; and a foaming chamber located downstream of the mixing chamber and in fluid communication with the air inlet and with an outlet of the mixing chamber, the foaming chamber housing a plurality of blades configured for rotation about a longitudinal centerline of the wand.

2. The wand of claim 1, further comprising, a dissolution chamber in fluid communication with the water inlet and an inlet of the mixing chamber, the dissolution chamber configured to house an at least partially solidified stick including the surface activation (cleaning) agent.

3. The wand of claim 2, further comprising, the dissolution chamber including a stick canister.

4. The wand of claim 3, further comprising, the stick canister including an extruder nozzle connected to a bottom of the stick canister.

5. The wand of claim 2, further comprising, the dissolution chamber including an injection manifold including an array of jet nozzles.

6. The wand of claim 2, further comprising, the dissolution chamber including a plunger-cylinder assembly arranged to move toward the at least partially solidified stick.

7. The wand of claim 2, further comprising, the dissolution chamber including a compressed air inlet.

8. The wand of claim 1, further comprising, a pressure regulator arranged to control an inlet water pressure to the wand.

9. The wand of claim 1, further comprising, the mixing chamber including at least one static mixer.

10. The wand of claim 9, wherein the at least one static mixer includes a porous packing material.

11. The wand of claim 9, wherein the at least one static mixer includes a metal mesh.

12. The wand of claim 9, wherein the at least one static mixer includes a gravel mixture.

13. The wand of claim 9, wherein the at least one static mixer includes an array of fixed baffles.

14. The wand of claim 1, further comprising, a nozzle exhaust located at an end of the wand opposite that of the water inlet and in fluid communication with an outlet of the foaming chamber.

15. A method for continuously delivering a surface activation (cleaning) agent on demand as foam, the method comprising: connecting a wand to a pressurized sources of water and air; generating foam on demand by flowing the water and air through the wand, the water dissolving a portion of one or more polymer sticks containing the surface activation (cleaning) agent; wherein the wand includes a water inlet configured for connection to a pressurized source of water; a mixing chamber located downstream of the water inlet; an air inlet configured for connection to a pressurized source of air; and a foaming chamber located downstream of the mixing chamber and in fluid communication with the air inlet and with an outlet of the mixing chamber, the foaming chamber housing a plurality of blades configured for rotation about a longitudinal centerline of the wand.

16. The method of claim 15, further comprising, controlling a speed of the rotation of the plurality of blades.

17. The method of claim 15, further comprising, controlling a pressure of the compressed air entering the foaming chamber.

18. The method of claim 15, wherein the wand further includes a dissolution chamber in fluid communication with the water inlet and an inlet of the mixing chamber, the dissolution chamber configured to house an at least partially solidified stick including the surface activation (cleaning) agent.

19. The method of claim 15, wherein the mixing chamber includes at least one static mixer.

20. The method of claim 15, wherein the wand further includes a nozzle exhaust located at an end of the wand opposite that of the water inlet and in fluid communication with an outlet of the foaming chamber.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a sketch showing an embodiment of the in situ foam generation apparatus. The apparatus is portable and in the form of a longitudinally extending wand including the dissolution, static mixing and foam generation chambers located between the water inlet end and nozzle exhaust end of the wand.

(2) FIG. 2 is a sketch showing one configuration of the dissolution chamber used to dissolve polymer sticks with completely solidified consistency.

(3) FIG. 3 is a sketch showing an alternative configuration of the dissolution chamber used to dissolve polymer sticks with partially solidified consistency.

(4) FIG. 4 is a sketch showing the foaming chamber used to generate soft foam by combining chemicals dissolved in water and compressed air.

ELEMENTS AND NUMBERING USED IN THE DRAWINGS AND DETAILED DESCRIPTION

(5) 10 In situ foam generation apparatus or wand 11 In-line water pressure regulator (also indicating the aqueous solution or water line) 12 Flange connector 13 Dissolution chamber 14 Mixing chamber 15 Compressed air line 16 Foaming chamber 17 Nozzle exhaust, hose jet or nozzle section 18 Polymer stick saturated with chemicals 19 Cavity or canister 20 Static mixer (array of baffles or porous packing material) 21 Injection manifold 22 Pressure jet nozzle 23 Plunger-cylinder assembly 24 Compressed air source 25 Fully solidified polymer stick 26 Reloading door 27 Dissolution chamber outlet 31 Polymer stick canister 32 Partially solidified polymer stick 33 Extruder nozzle 34 Plunger-cylinder assembly 35 Compressed air source 36 Dissolution chamber outlet 41 Agitator or mixing blades 42 Compressed air source

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(6) A preferred embodiment of an in-situ foam generation apparatus includes a dissolution chamber that houses one or more polymer sticks saturated with one or more cleaning agents that can be dissolved in water at different pressure settings and blown out as soft foam using compressed air, a mixing chamber arranged to receive the dissolved chemicals from the dissolution chamber, and a foaming chamber arranged to receive the mixed chemical-water mixture from the chamber and generate foam. The apparatus enables rapid and continuous generation of foam on-site and on-demand. Also, the apparatus can be easily tailored to utilize polymer sticks of different configurations (e.g., shape, size) based on the application. Moreover, polymer sticks of varying consistencies such as solidified and partially solidified can be used in this apparatus.

(7) Referring to FIG. 1, a preferred embodiment of an in-situ foam apparatus 10 includes a dissolution chamber 13, a mixing chamber 14 connected to an outlet of the dissolution chamber 13, and a foaming chamber 16 connected to the outlet of the mixing chamber 14. The dissolution chamber 13 includes a cavity or canister 19 (see also e.g., FIG. 3 at canister 31) that houses one or more polymer sticks 18 of the same or different composition.

(8) The polymer sticks 18 can be made of inorganic, environmentally safe, water-soluble chemicals mixed with surfactants, or their equivalent. The polymer stick 18 chemical configuration can be adjusted to specifically remove a particular type of dirt or residue, or a combination of residues from the equipment. In addition, the polymer stick 18 composition can be modified to obtain a varying end consistency like fully solidified or partially solidified states. The end consistency state should be such that it does not negatively affect the dissolution/foaming ability of the polymer sticks 18 or the cleaning efficacy of the loaded chemicals. Additionally, the shape of the polymer stick 18 can be any shape preferable, including but not limited cube, cuboid, parallellopied, or non-parallellopiped.

(9) As the polymer sticks 18 are dissolved in the dissolution chamber 13 using an aqueous solution such as water, the cleaning agents are released from the sticks 18. The volume fraction of base polymer and the cleaning agents can be any fraction preferable for a particular application. In a preferred embodiment, the volume fraction is 80:20 base polymer to cleaning agent. In addition to the chemical composition, the rate of polymer stick 18 dissolution and foam generation is dependent on the inlet pressure and operating temperature, both of which can be adjusted for a particular application.

(10) The dissolution chamber 13 is connected to an aqueous solution line through a flange connector 12. The aqueous solution line preferably delivers water to the chamber 13. The flow circuit contains an in-line water pressure regulator 11 which can be adjusted to vary the inlet water pressure, and will determine the rate and quality of foam generation.

(11) Referring to FIG. 2, the aqueous solution line is connected to an injection manifold 21 that is fabricated with an array of pressure jet nozzles 22 capable of delivering tightly grouped high-pressure water jets in a direction perpendicular to the water inlet. Preferably, manifold 21 is made out of corrosion resistant metal or plastic.

(12) A fully solidified polymer stick 25 is arranged above the manifold 21 toward an upper end of the dissolution chamber 13 and is directly exposed to the high-pressure water jets of the injection manifold 21.

(13) The polymer sticks 25 are loaded into the dissolution chamber 13 through the reloading door 26 at the upper end of the chamber 13. The distance between the injection manifold 21 and the polymer stick 25 can be adjusted by using a plunger-cylinder assembly 23 connected directly to the manifold 21, preferably operated by a compressed air source 24. Maintaining a constant distance between the manifold 21 and dissolving polymer stick 25 helps in uniform dissolution of the polymer stick 25 through the entire cycle. The uniformly dissolved polymer solution exits the dissolution chamber 13 at the dissolution chamber outlet 27.

(14) Referring to FIG. 3, another preferred embodiment of the dissolution chamber 13 is particularly suitable for handling partially solidified polymer sticks 32. Semi-solid polymer sticks 32 act like a shear-thinning medium that can flow under a constant shear stress. The partially solidified polymer stick 32 is loaded into a canister 31 located at an upper end of the dissolution chamber 13 and arranged perpendicular to the pressure-regulated water line (indicated by pressure regulator 11). An extruder nozzle 33 located at a bottom end of the canister 31 is placed with its outlet facing the downstream direction of the water flow (to prevent water from seeping back into the canister 31). A constant shear stress can be applied to the polymer stick 32 inside the canister 31 through a plunger-cylinder assembly 34 located at an upper end of the canister 31 and preferably operated by a compressed air source 35. The polymer stick 32 starts to flow out of the extruder nozzle 33 and dissolve into the water stream. Water with dissolved chemicals exit the dissolution chamber outlet 36 to enter mixing chamber 14.

(15) Referring to FIGS. 1 and 2, water with dissolved chemicals at the outlet 27 of dissolution chamber 13 is perfused through the mixing chamber 14. The mixing chamber 14 is preferably a static mixer 20 comprising an array of baffles engineered to uniformly mix the dissolved chemicals. Preferably, the baffles are made of corrosion resistant metal or plastic. Alternatively, the mixing chamber 14 is filled with a porous packing material such as, but not limited to, a metal mesh (preferably steel) or a non-reactive gravel mixture to facilitate uniform mixing of chemicals into water and act as static mixer 20. The major function of mixing chamber 14 is to disturb uniform flow lines of water and introduce turbulence in the flow to ensure uniform mixing of cleaning chemicals in water.

(16) Referring to FIGS. 1 and 4, the statically mixed chemical-water mixture exiting the mixing chamber 14 is then perfused through the foaming chamber 16, which is equipped with an agitator preferably in the form of a rotating mixer for final mixing and foam generation. Preferably, the rotating mixer is a series of turbine or mixing blades 41 suspended sequentially on a shaft in along the longitudinal centerline of the chamber 16. The mixing blades 41 are allowed to freely rotate about the center axis of the shaft. A pressure regulated compressed air source 42 is connected to the foaming chamber 16 and compressed air is delivered to the chamber 16 through compressed air line 15.

(17) Pressurized foaming chemicals entering foaming chamber 16 along with the compressed air drives the shaft which, in turn, facilitates the foam generation. The compressed air pressure can be varied to control different foam characteristics such as but not limited to the chemical concentration per unit foam area, foam air bubble stiffness, and surface tension of foam bubbles. The foamed chemical mixture is then passed through a hose jet or convergent nozzle section 17 (see FIG. 1). The sudden increase in pressure near the convergent throat results in generation of high turbulent energy which agitates the chemical mixture, and high quality foam is discharged through the outlet of section 17.

(18) The in situ foam generation apparatus 10, or at least one of its components, can be scaled up or down for specific applications. Some of the applications that could benefit from the deployment of the in situ foam generation apparatus 10 include but are not limited to (1) cleaning of fin and fan coolers in refineries, gas plants, gas transmission stations, chemical plants, geothermal power plants, and solar power plants; (2) cleaning of industrial radiators in natural gas compressors, engine driven air compressors, engine driven generators, and turbine oil coolers; (3) cleaning of air cooled compressors utilized in electric generation stations, and (4) cleaning of air conditioning evaporator coils.

(19) While preferred embodiments of surfactants/chemicals in a polymer stick form factor and an apparatus for in-situ foam generation have been described, a person of ordinary skill in the art understands that certain changes may be made in the details of construction and the arrangement of components without departing from the spirit and scope of this disclosure or the following claims.