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Procedyne fluid bed technology is primarily based on dense-phase fluidization, at the lower end of the fluidization regime. The low fluidizing velocities - and accordingly low gas flows - typically employed in Procedyne fluid bed systems translate to very effective, efficient and low-cost operation.
This capability for processing of very fine and/or lightweight materials arises from the unique design features we can employ. Prominent among these are:
Indirect Heating As Procedyne systems typically operate at very low gas flow rates, indirect heating of the process is possible. This feature allows for processing at bed temperatures up to 1200C, with capability to maintain specific atmospheric conditions. Virtually 100% of the process heat requirement is via the indirect through-wall radiant/convective heat transfer mechanism.
Integral High-Temperature Gas Filtration Even at very low gas velocities, elutriation of fine particles from the fluidized bed can be an issue. Procedyne has a solution in its high-temperature gas filtration system, which can be integral to the fluid bed process vessel, for virtually 100% solids retention in the process environment and particulate-free exhaust.
The complete physical separation of the heat source from the process imparts several distinct advantages, such as:
The test was preformed to illustrate the temperature uniformity achievable in a Procedyne fluid bed. The pilot unit is an indirectly-heated system, with capability for preheating of the fluidizing gas. In this test, no gas preheating was utilized, and the maximum bed temperature was targeted, to present the most difficult conditions for temperature uniformity.
The temperatures were recorded using a three-point measurement in a radial direction, with the points of measurement at the vessel centerline [A], vessel wall [C], and midpoint between the two [B]. The temperature probe was traversed in the axial direction from top to bottom (nominal 2" above the gas distributor) in 4" increments. Temperatures were recorded in the downward and upward traverses of the fluidized bed. The time duration for these traverses was roughly one hour. The data shown in the table below is from the downward traverse; the upward traverse yielded values within the tolerance displayed in the downward traverse
The mechanical agitation of the solids bed can often facilitate effective fluid bed processing of materials that otherwise would not be suitable, including fibers and flakes, and materials which tend to adhere or agglomerate.
These agitated units are available for both batch and continuous processors, large or small, and operating at low or high temperature.
Procedyne performs fluidization trials on all candidate materials, to determine the fluidizing characteristics of the material.