Case Study: Grinding Corn Germ for the Catalytic Extraction of Oil
January 1, 2009
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A thermal analysis of unprocessed germ was
performed to identify whether ambient or cryogenic grinding would be
recommended.
Corn oil typically is recovered from the corn germ through a solvent-based process using hexane. Due to capital equipment requirements and special handling and disposal considerations, the use of hexane is considered a rather expensive process. Unfortunately, water-based methods for oil recovery have not been successful because the yields of corn oil are much less than those obtained using hexane extraction.
Recently, researchers at the USDA’s Agricultural Research Services in
Philadelphia investigated the use of a combination of enzymes and an aqueous
system to extract oil from corn germ. The corn oil located within the germ is
contained in a starch-and-protein matrix in small inclusions with a nominal 1-μm
diameter. Because the primary function of the enzyme in the new process is to
depolymerize starch, grinding prior to extraction should accelerate the
extraction process and increase the oil yield.
A thermal analysis of the unprocessed germ was performed to identify whether ambient or cryogenic grinding would be recommended. The transition temperatures were measured on a differential scanning calorimeter (DSC). The DSC output shown in figure 1 identified a glass transition temperature (TG) for the starch component at around -72°F (-58°C) and a melting temperature (TM) for the oil component at around -4°F (-20°C). These results were consistent with literature values for similar materials. Therefore, based on the rather low TG, the material was considered appropriate for using cryogenic conditions in grinding to expose sufficient surface area to maximize the oil extractability.
Samples were tested in a pilot-scale process that incorporated a helical
screw conveyor in which LIN was added to the process (figures 2 and 3). The
corn germ then was passed through the grinding mill, and the powder
subsequently was separated from the resulting nitrogen gas in the cyclone
separator. Using nitrogen in this particular process provided a secondary
benefit of minimizing the oxidation of the oil fraction during processing.
The process conditions for the trial are summarized in the table. While the
LIN ratio often can be determined experimentally, the LIN requirement in this case
was calculated from the specific heat as a function of temperature (as
determined from the data in figure 1) and the measured temperature change
through the conveyor. The corn germ was cooled to the desired inlet temperature
of the grinding mill using LIN spray in a helical screw conveyor with a
retention time of five minutes. The mill inlet temperature shown in the table
is much lower than the material TG to compensate for the
heat input from the mechanical grinding process.
A representative particle size distribution is given in figure 4. The
resulting corn germ D50 value was 17.4 μm
for this sample, as taken downstream of the cyclone separator. The smallest
measured particle was 2.3 μm. Nonetheless, the injection of LIN into
the feed conveyor was an effective and efficient method of controlling the
in-feed temperature of the corn germ so that the desired temperature conditions
could be maintained throughout the grinding process. Furthermore, as the power
input to the sample was varied, it was possible to use dynamic control of the
LIN addition to maintain the desired processing conditions within the range
tested. This example illustrates the flexibility that can be achieved using a
LIN-based temperature control system.
Figure 1. A thermal analysis of raw corn germ as measured with a DSC Q1000 showed the TG and TM to be consistent with literature values for similar materials.
Corn oil typically is recovered from the corn germ through a solvent-based process using hexane. Due to capital equipment requirements and special handling and disposal considerations, the use of hexane is considered a rather expensive process. Unfortunately, water-based methods for oil recovery have not been successful because the yields of corn oil are much less than those obtained using hexane extraction.
Figure 2. Samples were tested in a LIN pilot-scale process that incorporated a helical screw conveyor.
A thermal analysis of the unprocessed germ was performed to identify whether ambient or cryogenic grinding would be recommended. The transition temperatures were measured on a differential scanning calorimeter (DSC). The DSC output shown in figure 1 identified a glass transition temperature (TG) for the starch component at around -72°F (-58°C) and a melting temperature (TM) for the oil component at around -4°F (-20°C). These results were consistent with literature values for similar materials. Therefore, based on the rather low TG, the material was considered appropriate for using cryogenic conditions in grinding to expose sufficient surface area to maximize the oil extractability.
Figure 3. The cylindrical tube at the top of the helical screw conveyor was fitted with a LIN injection manifold and appropriate controls to introduce the refrigerant into the process. The body of the conveyor was insulated to mitigate the cryogenic burn hazard and maximize cooling efficiency.
Figure 4. The particle size distribution for the cryogenically ground corn germ (as measured with a Horiba LA-910) demonstrated that LIN was an effective and efficient method of controlling in-feed temperature.
This table shows the average settings and run-time calculations for several Microtec UTM-200 corn germ trials conducted using LIN.
