Abstract:
A method for saturating a thermoplastic polymer material includes continuously moving the polymer material through a pressurized pressure vessel. To do this, the method includes sealing the pressure vessel with a series of dynamic seals that allows the polymer material to continuously move through the pressure vessel while maintaining the pressure inside the pressure vessel.

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
       [0001]    The present application claims the benefit of U.S. Provisional Patent Application No. 62/212,251, filed Aug. 31, 2015, which is incorporated by reference herein in its entirety. 
     
    
     FIELD OF THE DISCLOSURE 
       [0002]    Saturation of plastic is typically achieved by placing the plastic in a high pressure gas environment (inside a pressure vessel) for an amount of time so that the plastic can absorb some of the gas. The system and method disclosed herein allows continuous saturation of plastic, which can be, for example, a polymer or polymeric material, by placing a series of dynamic seals at each end of a pressure vessel. Plastic polymer material enters the pressure vessel via the system of seals, and exits the pressure vessel saturated with gas via a system of seals. 
       BACKGROUND 
       [0003]    Solid-state microcellular processing is a well-known art involving a two-stage batch process. In the first stage (absorption), a solid polymer is saturated with high pressure inert gas (e.g., CO2) in a pressure vessel until a desired gas concentration level is achieved throughout the polymer matrix. Once the gas-polymer mixture is removed from the pressure vessel into ambient environment (desorption), a supersaturated specimen is produced that is thermodynamically unstable due to the excessive diffusion of gas into the polymer. In the second stage (foaming), the gas-polymer mixture is heated in a hot water bath or some other heating medium (non-limiting examples of which include hot air, steam, infrared radiation, etc.) at a temperature close to the glass transition temperature (Tg) of the gas-polymer mixture in order to induce microcellular bubble nucleation and growth. 
         [0004]    Saturation of polymer rolls requires placement of an interleaving layer between layers of polymer, to allow gas to enter the surface of the polymer evenly. The addition of this layer is an added process step, and the removal of the interleavement is yet another process step. 
         [0005]    Repeated opening and closing of pressure vessels wastes large amounts of high pressure gas, and also creates pauses in plastic processing. A roll that is removed from a pressure vessel begins to lose gas immediately. Gas diffuses out into the atmosphere from the exterior of the roll first and the interior of the roll last. Hence, there may be difficulty achieving consistent foaming behavior throughout the roll, particularly in polymers that lose gas quickly. 
         [0006]    U.S. Pat. No. 5,158,986 discloses a method of passing an extruded thermoplastic material from a gas-saturation chamber to a foaming chamber via a time-controlled system of rollers. Dynamic seals are stationed between the chambers to allow passage of the thermoplastic sheet while preserving the environmental conditions of each chamber. To date, however, there is no engineering solution for manufacturing a dynamic seal that can operate at pressures required for practicing the art referenced in this current patent. 
       BRIEF SUMMARY 
       [0007]    In one aspect, illustrative embodiments in accordance with the present disclosure relate to a method of saturating a polymeric material with pressurized gas in a pressure vessel. The method comprises continuously passing a solid polymeric material through a first set of cascading seals at an inlet to the pressure chamber, exposing the solid polymeric material passing through the pressure vessel to pressurized inert gas to form a saturated solid polymeric material, and continuously passing the saturated solid polymeric material through a second set of cascading seals at an outlet to the pressure chamber. 
         [0008]    In another aspect, illustrative embodiments in accordance with the present disclosure relate to a system for saturating a solid polymeric material with gas. The system comprises a pressure vessel defining an interior and having an inlet and an outlet fluidly coupled to the interior. The pressure vessel further comprises a pump fluidly coupled to the interior to supply pressurized gas to the interior, a first set of cascading seals fluidly sealing the inlet, and a second set of cascading seals fluidly sealing the outlet. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0009]    In the drawings: 
           [0010]      FIG. 1  is a schematic view of a series of dynamic seals that can be included in a polymer saturation system of  FIG. 2  according to an embodiment of the present disclosure. 
           [0011]      FIG. 2  is a schematic view of a polymer saturation system according to an embodiment of the present disclosure. 
       
    
    
     DETAILED DESCRIPTION 
       [0012]      FIG. 2  is a schematic illustration showing a polymer saturation system  10  incorporating the cascading seals  20 A,  20 B. A polymer or polymeric material  12  enters the system  10 , more specifically entering an interior  24  of a pressure vessel  22 , at one end (from the left side of the drawing), illustrated by arrow  14 , and exits as a saturated polymer material  12 B at the other end (to the right of the drawing), illustrated by arrow  16 . Pressure in each section of the system  10  may be maintained by a pressure regulation system  18 . This pressure regulation system  18  could either be, by way of non-limiting example, an external gas source that adds high pressure gas to the system (while excess gas pressure is vented), or an active pump system that both pressurizes and depressurizes one or more sections of the system  10 . 
         [0013]      FIG. 1  shows a schematic illustration of a series of dynamic seals  20 A (cascading seals) and the pressure differential across each seal  20 A as a portion of total pressure inside the interior  24  of the pressure vessel  22 . Polymer material  12  enters the series of dynamic seals  20 A (from the left side of the illustration, as illustrated by arrow  14 ), and then exits the dynamic seals to enter into the interior  24  of the pressure vessel  22 . Pressures P 1 , P 2 , P 3 , and P 4  are each a fraction of the total difference in pressure between P ambient and Pmax, and are maintained at their required pressure P 1 , P 2 , P 3  and P 4 , respectively, by a pressure regulation system  18  ( FIG. 2 ), which can be, in non-limiting example, an external system of pumps or other source of high pressure gas. For example, in a pressure vessel  22  containing 500 psig, each seal  20 A might be used to maintain a pressure differential of 100 psi. P 1  would equal 100 psig, P 2  would equal 200 psig, P 3  would equal 300 psig, P 4  would equal 400 psig and Pmax would equal 500 psig. In other embodiments, the total number of seals  20 A included in the series of dynamic seals  20 A may be more or less than five. In addition, the pressure differential across each seal  20 A may not be equal. For example, in order to reduce the amount of gas that escapes into the environment, it may be desirable to maintain P 1  at a low level, such as 5 psig, and to maintain the P 2  at a higher level, such as 50 psig. The total number of seals  20 A required could also be determined by the maximum pressure differential allowable across each seal  20 A. A similar system of seals  20 B ( FIG. 2 ) may be used on the exit end. 
         [0014]    A method for continuous processing of a polymer material  12 , non-limiting examples of which can include polymer sheets, rods, fibers, or any continuous thermoplastic part, includes using a pressure vessel  22  having cascading seals  20 A,  20 B on each end to maintain substantial pressure inside the interior  24  of the pressure vessel  22  while the polymer material  12  moves through the interior  24  of the pressure vessel  22 . The cascading seals  20 A,  20 B, which allow the plastic to enter a high pressure environment, include a series of dynamic seals  20 A,  20 B, each operating at a differential pressure which is only a fraction of the total pressure (Pmax) in the interior  24  of the pressure vessel  22 . The saturation system  10  could be placed in series after a roll of plastic polymer material  12  or after an extruder whereby the plastic polymer material is taken up by the saturation system  10  as according to the schematics in  FIG. 2 . The saturation system  10  can also be placed before any plastic polymer material processing equipment or machinery, including, by way of non-limiting example, an air oven, thermoformer, and material uptake machine, that may be used to process or store the saturated polymer material  12 B. 
         [0015]    To the extent not already described, the different features and structures of the various embodiments can be used in combination with each other as desired. That one feature may not be illustrated in all of the embodiments is not meant to be construed that it cannot be, but is done for brevity of description. Thus, the various features of the different embodiments can be mixed and matched as desired to form new embodiments, whether or not the new embodiments are expressly described. 
         [0016]    While the present disclosure has been specifically described in connection with certain specific embodiments thereof, it is to be understood that this is by way of illustration and not of limitation. Reasonable variation and modification are possible within the scope of the forgoing disclosure and drawings without departing from the spirit of the present disclosure which is defined in the appended claims.