- minerals and ores
- ceramics
- inorganic pigments
- carbons
Procedyne systems operate on electricity, natural gas, or fuel oil, and are highly efficient, even at high temperature.
Precise temperature control, combined with uniform and complete fluidization, provide for reproducible, high-quality product with extremely high yield.
An array of batch and continuous calciners can be custom-designed to each application.
- Fine Particle Processing
- Batch Processors
- Continuous Processors
- Indirect Heating
- Direct Heating
- Temperature Uniformity
- Mechanical Agitation
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Procedyne's unique fluid bed technology is ideal for fluid bed processing of even very finely divided, and/or lightweight materials. Materials with particle sizes as small as single-digit micron and densities as low as 0.02 g/cc can be successfully handled.
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
Integral High-Temperature Gas Filtration |
N/A Procedyne designs and builds batch fluid bed processors for drying, calcining, activations and other chemical processes. Batch units are typically cylindrical in shape, and can be configured with a range of accessories and ancillary equipment. Designs range from low-temperature units operating at only slightly elevated temperature, to units operating at nominal 1200°C bed temperature. We can supply small bench- or lab-scale systems from few inches in diameter, up to large commercial systems exceeding 10' in diameter. |
N/A Procedyne designs and builds continuous fluid bed processors for drying, calcining, activations and other chemical processes. Batch units are either cylindrical in shape, for a back-mixed processing method, or trough (rectangular) for a plug-flow processing method. For continuous processes requiring very tight approximation of true plug flow, with exacting residence time requirements, we offer a specialized configuration of a trough-style processor - our multi-stage continuous processor. Continuous processors can be configured with a range of accessories and ancillary equipment. Designs range from low-temperature units operating at only slightly elevated temperature, to units operating at nominal 1200°C bed temperature. We can supply small bench- or lab-scale systems for a few kg/hr up to units providing capacities in the tons per hour magnitude. |
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With the typically-low gas flows utilized in our fluid bed systems, indirect heating of the process is possible. The indirect heating mechanism maintains complete physical separation of the heat source and the thermal process being facilitated.
The complete physical separation of the heat source from the process imparts several distinct advantages, such as:
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Bed Temperature Uniformity Test Data
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The data presented was obtained in a test program in Procedyne's 20" diameter cylindrical pilot fluid bed processor at the Procedyne Process Technology Laboratory.
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 |
Vessel Diameter |
N/A 20 in |
Depth of Fluidized Bed |
N/A 24 in |
Bed Material |
N/A Aluminum Oxide |
Particle Size |
N/A 150 mesh |
Bulk Density |
N/A 110 lb/cu ft |
Table |
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Minimum Temperature |
N/A 1157.8°C |
Maximum Temperature |
N/A 1161.0°C |
Temperature Spread |
N/A 3.2°C |
Average Temperature |
N/A 1159.7°C |
Standard Deviation |
N/A 0.746°C |
Coefficient of Variance |
N/A 0.064% |
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For processing of materials which exhibit less-than-ideal fluidization characteristics, Procedyne offers mechanically agitated fluid bed processors. These units employ an internal, typically-low-speed, motor-driven agitator to assist with the gas-phase fluidization of the solids material.
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.
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