Referring to
Over all ventilation of the almond pasteurizing apparatus is required. Ventilation apparatus 4 includes vacuum blower 40 having inlet line 47. The inlet line 47 communicates to steam ladder cyclone separator 41 and drying ladder cyclone separator 42. These respective separators have their airlocks 43, 45 for the evacuation of accumulated debris. Steam ladder cyclone separator 41 includes cyclone separator inlet 44 overlying steam ladder 1. Likewise, drying ladder cyclone separator 42 includes drying ladder cyclone separator inlet 46 overlying drying ladder 2. In this manner, systematic ventilation of the apparatus here disclosed occurs.
Referring to
Referring to
Steam ladder 1 includes an upper oil jacket enclosed steam ladder 10 and a lower open steam ladder 11. Regarding upper enclosed steam ladder 10, the structure consists of enclosed alternating inclined surfaces 19. As in such traditional ladder structures, almonds slide on their major surfaces from the top of the ladder to the bottom of the ladder. Steam nozzle 12 introduces steam at up to 500 degrees Fahrenheit. Upper enclosed steam ladder 10 is dimensioned to enable almonds to have a 4 second to dwell time and be heated to a temperature on the surface of the almonds of at least 160 degrees Fahrenheit. This produces the required sterilization without changing the chemical and taste properties of the almonds.
Upper enclosed steam ladder 10 is surrounded by heated oil jacket 14. The heated oil jacket 14 includes jacket steam heaters 15. Steam inflow through the jacket steam heaters 15 maintains oil within oil jacket 14 about upper enclosed steam ladder 10 at an elevated temperature to assure pasteurization. Insulation covers 16 on the sides of upper enclosed steam ladder 10 prevent unnecessary heat loss from oil and steam.
Pasteurized but moist almond product is metered to drying ladder airlock 32. The drying ladder airlock 32 in turn feeds the moist pasteurized almond product to drying ladder 2. The drying ladder 2 consists of the first drying ladder segment 21 and second drying ladder segment 22. First drying ladder segment 21 has first drying ladder incline surfaces 23. Second drying ladder segment 22 has second drying ladder incline surfaces 24. These respective incline surfaces alternate so that almonds slighting down first drying ladder incline surfaces 23, and fall on to a second drying ladder incline surface 24. In this way the almonds alternatively slide on their alternate major surfaces down the respective incline surfaces.
The respective first drying ladder segment 21 and second drying ladder segment 22 are open structures. That is to say, the areas between the respective incline surfaces 23, 24 are open. Referring briefly to
It is been found that provision must be made for respective cleaning of steam ladder 1 and drying ladder 2. Steam ladder 1 is cleaned by opening end doors 19. See
Referring to
The reader will understand that modification of this invention can occur. For the broad practice of the technique here disclosed, all that is required is that the almonds be exposed to pasteurizing steam in a vertical conduit for the requisite period of time and temperature followed by a drying step. For example, we have tried counter flow of both steam and drying air to the falling almonds. Moreover, while we show parallel flow of steam with the almond product, the reader will understand that both cross flow and counter flow of steam to the almond product is operable. Additionally, as of this writing we are considering heating the oil for the oil jacket surrounding the ladder exterior to the oil jacket in a separate heater. This heating can be in addition to the heating here shown with steam lines passing through the jacket. What is illustrated here is the preferred embodiment as of time of the drafting of this patent application.
As of the filing of this Provisional Patent Application, this apparatus was under actual test. While a successful test has not been run with the parameters set forth above, testing indicates that the concept is viable. Accordingly, it has been determined that additional heat energy will be required for sterilization, the parameters of which can be readily determined.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US04/16178 | 5/20/2004 | WO | 00 | 1/26/2007 |
Number | Date | Country | |
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60473276 | May 2003 | US |