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operated at atmospheric pressure in con­  This component is then mixed with a   units. Depending on the application,
           ventional foaming.                 second pre-mixed blend of additional   such units can be further engineered to
             Depending upon the chemical char­  polyol, catalyst, surfactants, and blow­  include the use of computerized con­
           acteristics of both the isocyanate and the   ing agent.               trols, curing ovens, and pour stations.
           resin, either a rigid or a flexible foam                              Various bulletins and technical articles
           can be produced. By varying the form­  PROCESSING EQUIPMENT           are also available from vendors to aid
           ulation, it is also possible to produce a                             in equipment selection and efficient
           foam exhibiting any degree of flexibility   The basic foam machine consists of   operation.1*2
           between the two extremes. Generally,   supply vessels, supply and recirculating   In the spraying process, there are
           flexible urethane foam is processed by   lines, metering pumps with variable   two general classes of spray guns. One
           the conventional foaming method as a   throughput, an integral valve block, a   class uses internal mixing, either dy­
           pourable liquid, while rigid urethane   mixing head, nozzle, and solvent flush   namic or static; the other uses external
           foam is processed by either method.  system. The prime requisite of the ma­  mixing. The dynamic internal mix
                                              chine is the ability to deliver a specific   guns have advantages over static types
                                              quantity of components accurately and
           THE PHYSICAL PROCESS                                                  in providing better mixing and ease of
                                              reproducibly for any period of time.   conversion to pour application. The
             There are currently two basic proc­  Since some of the reaction mixture re­  major problems of this type gun are
           esses by which polyurethane foam is   mains in the mixing chamber after each   excessive weight and gun plugging but
           produced. The first is the “One Shot   pour, the residual foam mix must be   by using proper solvent flushes the plug­
           Process” in which all the ingredients are   flushed when the time between shots is   ging problem can be minimized. This
           piped separately into the mixing head   longer than the cream-time of the ma­  equipment is preferred for spraying the
           (Figure 2). To streamline the process,   terial. Nonflammable solvents such as   one-shot foam system. Static type in­
           a new one shot system (Figure 3) is in   methylene chloride and 1,1,1 trichloroe­  ternal mix guns are available as high-
           use which pre-combines certain of the   thane function satisfactorily for this  pressure, airless, spray-through injection
           components upstream of the mixing   purpose. Acetone is also used.    nozzles. The principal advantage of the
           head. This reduces the number of     The complexity of the equipment re­  airless gun is minimization of over-spray
           separate lines entering the mixing head   quired for the production of urethane   with attendant reduction of isocyanate
           from six or seven to only three or four.  foam depends on whether it is frothed,   exposure and loss of material. The
             The second process is the “Pre-Poly­  sprayed or poured, and whether it is   external mix guns have the advantage
           mer Process” (Figure 4) whereby a   being factory or field applied. Almost   of requiring less maintenance because
           portion of the polyol is pre-reacted with   all equipment suppliers offer fully en­  they have no moving parts, require no
           an isocyanate to form a pre-polymer.  gineered pumping, metering, and mixing   solvent flush, and are less prone to

               Figure 2. One-Shot Process (Original)
                                    Ingredients (resin, catalyst, isocyanate, etc.)
                                    piped separately to mixing head. Some premixing can he done
                                    hy components into the resin upstream of the mixing head.

                  _Polyol - WO parts by.wgt.
                   (Polyesters or polyethers)                  i

                   isocyanate - 40-65 parts by wgj,
                                                 HO - R- OH * OCH-R-HCO
                   (Toluene diisocyanate — TDI    (Polyol) ^(Isocyanate)
                   Diphenylmefhane dl isocyanate—MDI
                   Polymethyl polyphenyl Isocyanate-   HO-R                                ■ red
                   Catalyst            PAP. I)                                        Pre -cure oven
                                                                                      (270-300'F)
                   (Tertiary amines ex.             Mixing head
                    Triethy famine diamine)
                  Fluorocarbon
                   (Blowing agent)




                          Crush roils          Product inspection?                      Convective heat
                         (For mechanical       mold cleaning and                            oven
                         conditioning to      . coating                                 (300° F, about
                         reduce set)                                                    6 min. retention
                                                                                        time)

                                                    To packaging
                        Post cure oven
                        (To develop mechanical
                        properties such as tensile
                        strength, firmness}                                          i
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