Combine
Yield Monitor Test Facility Development
T.F.
Burks, S.A. Shearer, C. J. Sobolik, and J.P. Fulton
Burks, T.F., S.A. Shearer, C. J. Sobolik, and J.P. Fulton. 2000. Combine Yield Monitor Test Facility Development. ASAE Paper No. 001084. Annual International Meeting, Midwest Express Center, Milwaukee, Wisconsin, July 9-12.
Abstract
The performance of the Yield Monitor Test Facility was positive, although a few limitation have been identified. First, it was found that the grain metering system can accurately meter grain at varying flows to a clean grain elevator with excellent accuracy over a prescribed period of time. A potential concern is whether or not the grain flow to the yield monitor force-impetus sensor is instantaneously uniform, or are there flow ripples generated in the grain handling system. Secondly, the weigh scale system appears to be very accurate in measuring the accumulated mass flow in the system. However, the potential for grain stream dynamics, tank vibration and load cell hysteresis confounds attempts to measure instantaneous grain flow at small flow rates ( 1 to 4 kg/s). Thirdly, the a commercially available yield monitor flow sensor demonstrated excellent accuracy across a range of static flow rates ranging from 1.3 to 21.1 kg/s. When considering accumulated mass flow, the percent difference between yield monitor and the weigh scale were less then 1% at calibration flow rates and approximately 3% for extreme flow rates. Variations in instantaneous mass flow rate logged by the yield monitor were observed to be approximately 8% at mean calibration flow rate.
Introduction
Yield monitor accuracy has been the focus of numerous
field investigations over the last several years. Accurate crop yield data
must be obtained so that producers can make informed crop production
decisions. Significant errors in crop yield prediction can adversely affect
any attempts to manage crop production. Perez-Munoz and Colvin (1994) noted
that yield monitors tend to overestimate crop yield in regions of low yield.
Development of the Yield Monitor Test Facility was motivated by the need for
producers to have confidence in yield monitor technology.
Literature
Review
A study was conducted by Shearer et al. (1997) in which
four combines (two John Deere 9500's, a Gleaner R70 and a Case IH 1680) were
used to harvest wheat with in the same field. Each combine was equipped with
yield monitors, the John Deere’s used GreenStar® and the other combines
used the Ag Leader 2000. The data from each combine was imported into a
popular mapping package to compare the yield estimates. They found that
significant differences in measured yield existed between adjacent harvest
swaths. These differences were attributed to potential machine/operator
variability. In response to these differences, they developed data filtering
techniques to help minimize the influence of calibration and machine/operator
differences. They concluded that machine calibration techniques were critical
in multiple-combine harvest systems.
In a study conducted by Kettle and Peterson (1998), it
was observed that the accuracy of combine yield monitors were significantly
effected by hill-side conditions and variation in harvest rates. Test were
conducted on two John Deere combines equipped with Greenstar® in the hilly
Palouse region of northern Idaho. They observed that the yield monitor’s
response to variation in inflow was exponential rather than linear and
suggested that calibration should been done at several operating points rather
than the traditional two point method. The observed yield monitor error was
20.3% when operating the combine at 1/3 the calibration through-put and 5.7%
at half the calibration through-put. They also found that the error in yield
monitor estimates were as high as 18.2% when harvesting uphill and 60.7% when
harvesting downhill, on 6 to 9% slopes. Finally, they found a very weak
correlation between the yield monitor estimates and hand samples (R2
=0.203) indicating that the yield monitor is not as sensitive to local
variation in crop yield.
Arslan and Colvin (1998) reported the development of a
test stand for combine grain yield monitors. They constructed a facility to
compare the accuracy of a yield monitor to an electronic scale. The found
strong correlations between the measured flow in the yield monitor and the
electronic scale (R2 =0.99). They observed stronger agreement when
testing at higher flow rates over longer durations.
A
test facility has been developed by Kormann et al. (1998) to test multiple
clean grain elevator yield monitors simultaneously. A system was built using a
Massey Ferguson 38/40 elevator with three reference yield systems installed,
the RDS Ceres II volumetric meter, and the MF Flow-Control and the Ag Leader
2000 mass flow sensors. A second elevator was placed in series with the first
elevator and was equipped with the CLASS Quantimeter II. It should be noted
that this system did not use the clean grain elevator fountain auger on either
of the elevators. The system was designed so that the elevators could be
tilted up to 15°
forward or aft with the potential for a simultaneous tilt of 15° to port or
starboard. In addition, provision was made to vary mass flow rate from 1
ton/hr to 35 ton/hr. They conducted test varying the inflow rate from 10 to 35
ton./hr and found mean calibration errors less than 3%. Only at the lowest
level did they experience error of up to 7%. The volumetric sensors tended to
perform better under low flow conditions then did the mass flow sensors. A
second set of test were conducted by varying the tilt of the elevator system.
They found mean errors up to 6% with standard deviations of up to 6%. The
radiometric MF Flowcontrol device performed the best of all sensors with mean
errors less than 2%, while the other sensors performed as follows from most to
least accurate; CLASS Quantimeter II (<3%), AG Leader 2000 (<4%) and RDS
Ceres II (<6%).
Facility
and Research Objectives
The
objectives for the Yield Monitor Test Facility development were as follows:
1.To develop a material
handling and weigh tank system capable of storing 17.5 cubic meters (500 Bu.)
of grain and provide grain flow to and from the clean grain elevator at rates
up to 158 cubic meters per hour (4500 Bu/hr).
2. To develop a grain metering system capable of accurately varying
grain flow from 2 to 158 cubic meters per hour ( 50 to 4500 Bu/hr) to the
clean grain elevator with feedback measurement of the volumetric delivery.
3. Develop an elevator support fixture capable of simulating hill-side
conditions typically experienced by grain combines (forward to aft, and port
to starboard pitch of 12 degrees
or 21% slope).
4. To develop a control and data logging system capable of generating a
range of flow conditions and gathering data from the grain meter volumetric
flow, the clean grain elevator yield monitor’s measured flow and the weigh
tank’s measured accumulated mass at a one second sampling rate.
The
research objectives for this paper were primarily associated with calibrating
and characterizing system performance, and comparing mass flow measurement
capability of the test facility with that of a commercially available yield
monitor system under variation in grain flow at static set points. The
specific research objectives were:
1. To calibrate weigh
scale and grain metering system;
2.
To quantify flow characteristic of system; i.e. transport delay and
sensitivity to flow levels; and
3.
To compare the performance of the test facility with a commercially available
yield monitor under variation in static grain flow levels ranging from 1.3 to
21.1 kg/s.
Component
and System Design
Conceptual
Design
There were several key features which guided the
development of the yield monitor test facility. First, it was desired to build
a laboratory system that could handle up to 17 m3 of grain in batch
storage and be housed in a laboratory. The system needed to be able to
transfer grain from a supply tank to the clean grain elevator and then on to a
receiving tank equipped with weigh scales. The grain must then be
re-circulated to the supply tank for further test runs. One of the facilities
design criteria was to dynamically change the elevator inflow rates. The flow
rate design range was established at approximately 2 to 159 m3/hr
for dry grain with a reasonable limit of 95 m3/hr for high moisture
grain. This wide flow regime is in response to studies by Kormann et al.
(1998) where errors up to 7% were observed in force impetus yield monitors
under low inflow conditions of 10 metric tons per hour. Finally, as reported
in the works of Kettle and Peterson (1998), yield monitor performance under
hillside conditions has been identified as a source of up 60% yield error when
combining in downhill conditions of 6 to 9% slope. As a result, the test
facility was designed to accommodate up to 21% slopes (12 degree) in the
forward, aft, port and starboard directions as well as a combination.
Grain
Handling System
The grain handling system was designed to hold up to 17.6
m3 of grain and is capable of flow rates up to 159 m3/hr
of dry grain. The system plan view is shown in Figure 1
and digitized slide of the over all system is shown in Figure
2. The system consists of two 2.8 m diameter, two ring tall Brock hopper
tanks. The supply tank was used to hold all of the grain prior to the start of
each test. The receiving tank is support on a frame which is in turn equally
supported by four 4500 kg load cells. Grain leaves the supply through a 30 cm
diameter supply auger which is powered by a 2.2 kW Allen-Bradley AC variable
speed motor drive. The grain is discharged into a volumetric grain metering
device which consist of a surge hopper and two flow control turrets. The first
turret is approximately 46 cm long and runs at 1.8 to 15.9 m3/hr
through the use of a 0.75 kW Allen-Bradley AC variable speed drive. The second
turret is 91 cm long, powered by a 1.5 kW Allen-Bradley AC variable speed
drive and runs at 15.9 to 159 m3/hr.
The grain meter is equipped with level control so that the 30 cm supply auger
is operated intermittently as grain is metered out of the supply tank. The
grain is transferred from the meter into a 25 cm horizontal auger which feeds
the supply elevator. The supply elevator operates at a constant speed of
approximately 400 rpm using a 5.6 kW AC motor and is capable of capacities of
up to 159 m3/hr. Grain discharges from the supply auger into the 25
cm clean grain elevator infeed auger. The spouting connection in between the
supply elevator and the clean grain elevator infeed auger is constructed of 25
cm diameter wire re-inforced flexible PVC duct to allow for hillside
simulation motion of the clean grain elevator.
Once the grain enters the clean grain elevator it travels
through the normal path of grain and discharges from the top of the fountain
auger into a suspended catch hopper. The clean grain elevator is powered by a
variable speed 15 kW hydraulic motor provided by White Hydraulics. The speed
of the hydraulic motor is approximately 400 rpm and is controlled by a
laboratory hydraulic test bench. This hopper discharges the grain into another
25 cm flexible spout, which discharges into a 30 cm U-trough. The U-trough
operates at approximately 190 rpm and is powered by a 2.2 kW electric motor.
The U-trough moves the grain up to a discharge point above the grain pump. The
25 cm grain pump is manufactured by Hutchinson and is capable of flow rates up
211 m3/hr of dry grain. It is powered by a 15 kW electric motor
with a chain speed of 100 m/s. The grain pump elevates and discharges the
grain into the receiving tank where weight data is being sampled once per
second. The grain pump is also used to move the grain from the receiving tank
back to the supply tank for repeat testing.
Grain Metering
The
grain metering device consist of a surge hopper and two flow control turrets.
The grain meter surge bin is capable of holding up 1 m3 of grain,
refer to Figure 3. The first turret is approximately
46 cm (M1), runs between 1.8 to 15.9 m3/hr, and is powered by a
0.75 kW AC variable speed drive. The second turret is 91 cm long (M2), powered
by a 1.5 kW AC variable speed drive and runs between 15.9 and 159 m3/hr.
Each drive system consists of a 1750 RPM motor, a direct coupled 90° gear reducer, and a
chain and sprocket drive linkage to provide the final speed reduction. M1 runs
at approximately 7 RPM to give 15.9 m3 /hr and M2 runs at
approximately 36 RPM to give 159 m3/hr.
The flow meter motor is powered by an Allen-Bradley AC variable speed
inverter drive which is in turn controlled by a 0 to 10 V speed reference
signal provided by the SLC-500 programmable controller. The variable speed
drive is capable of
a 10:1 speed reduction as the motor frequency is varied from 60 to 6
Hz, with constant torque throughout the speed range.
Each
meter has a low level sensor, while a single sensor serves to detect high
level in the surge hopper. Grain level is maintained approximately in between
the high and low levels. All three level sensors are 18 mm capacitive
proximity switches manufactured by Carlo Gavazzi. In addition, each turret
motor shaft speed is monitored using a 12 mm inductive proximity switch (Altech
Corp) which picks up the rotation of a shaft coupler fitted with two lugs
located 180 degrees apart. Each revolution of the turret motor shaft generates
two 24 volt DC pulses. This pulse train is conditioned by an optical isolator
and a de-bouncing circuit to provide a clean TTL signal. The shaft speed is
measured using a Keithley CTM05 counter card which runs in the background on
the system PC. The shaft speed is used to confirm the volumetric delivery of
grain from the meter. Meter flow is calibrated for each specific grain type.
Elevator
Support and Hillside Simulation Fixture
The
clean grain elevator from a John Deere 9600 combine was installed in a fixture
which was designed for simulating hillside conditions. The fixture consists of
the following components; a pitch and yaw pivoting support base, hydraulic
cylinder mounting brackets and supports; hydraulic motor assembly to drive the
elevator; elevator support tower; elevator infeed hopper; discharge grain
collection hopper and flexible spouting. The base consists of a steel floor
support stand which is rigidly attached to a 10 cm x 10 cm x 2.5 cm steel base
plate which is in turn fixed to the concrete floor using epoxy adhesive anchor
bolts. A fixed 5 cm diameter shaft is located at the top of the floor support
stand. A rectangular steel tube support frame is mounted horizontally on the
pitch shaft using a sleeve bearing at each end of the shaft. This shaft allows
the elevator to pitch in order to simulate forward to aft motion. Another
shaft is mounted on top of the support frame (rotated 90°
from the pitch shaft) using two additional sleeve bearings to provide yaw
rotation in order to simulate port to starboard motion. The elevator support
tower sets on top of the yaw shaft and is attached to the sleeve bearings. The
support tower serves to hold the clean grain elevator, the infeed hopper, the
hydraulic motor, and the discharge grain collection hopper in place. It is
constructed out of structural steel tubing.
The
hillside simulation fixture is capable of pitch and yaw of 15°
in either directions and can accommodate simultaneous pitch and yaw. In its
present configuration, the axes are rotated and held in position by
turnbuckles. However, it is intended that the system will be enhanced with the
addition of hydraulic cylinders which will allow for dynamic testing of
hillside conditions for the clean grain elevator.
Control System
and Instrumentation
The control system for the grain handling system was
developed for two levels of operation. First, the system was designed to run
under manual control from the motor control center, where the motor contactors
are controlled through a traditional pushbutton switch and relay system. Each
motor was provided with an individual circuit breaker and motor starter/heater
unit. Emergency stop and motor overload protection were provided to disable
the system if a motor overheats or if the emergency stop is pushed. This
manual mode of operation was provided for maintenance and emergency operation.
The second level of control was developed to provide automated control of the
start up process, level and speed control for the grain meter, systems
monitoring, data acquisition, dynamic grain inflow simulation and dynamic
hillside condition simulation. A three position switch is used to select
between manual and automatic system operation. The Yield Monitor Test Facility
control system hierarchy is shown in Figure 4. The
automated control system consists of a Allen-Bradley SLC-500 programmable
logic controller for machine systems control, and a Gateway 2000 Pentium
personal computer which serves as the User Interface Terminal (UIT) and as the
Data Acquisition System (DAS). The UIT was programmed in Visual Basic 6.0 with
the use of Allen-Bradley’s RSToolsTM, Computer Board’s
Universal Library and Keithly’s DriverLINX ActiveX controls. This software
were used to develop the user interface screens for both motor control and
data acquisition control. A typical Visual basic interface screen is shown in Figure
5 for the automatic start control and grain flow parameter selection.The
SLC-500 was programmed in ladder logic using Allen-Bradley’s RSLogix 500TM
to control all of the grain
handling system functions.
The primary components of the data acquisition system
were the Pentium PC, a Computerboards’ CIO-DAS801 analog card and a Keithley
CTM05 counter card. The PC was as a user interface to the data acquisition
system and for data storage. The principal data variables were the four
receiving tank load cell weights, the tare weight prior to grain flow,
the grain meter shaft speeds, and an interrupt driven running clock for
assisting in data synchronization. A synchronization signal is sent to the
yield monitor undergoing testing to initiate data acquisition simultaneously
with the start of data collection in the PC based system. This signal assists
in associating the weigh scale and meter data with the yield monitor data.
However, future enhancements will incorporate the GPS time into the PC based
data acquisition for precise synchronization.
The receiving tank was instrumented with four 4500 kg
load cells which supported the bulk tank and its support frame. Each load cell
was calibrated at the factory to a response range of 3.0 mV/volt of excitation
at full scale loading. The load cells were matched and calibrated in the laboratory with a load cell transmitter. The
transmitter provided zero offset and gain adjustment. It also provides a
stable 10 V DC excitation voltage to the load cell with line length
compensation. Additionally, the transmitter provides a scaled 4 to 20 mA
output signal which provides a more robust signal in the presence of potential
RF noise produced by the AC inverters. The load cell signals are transmitted
to the CIO-DAS801 for data acquisition. The four signals are combined to give
a tank weight which can be used to monitor the flow of grain through the
system.
The grain meter shaft speeds are used to determine the
volumetric flow rate of grain being supplied to the clean grain elevator .
Each turret motor has a shaft speed sensing unit, which consist of a special
dual pick-up shaft coupling and a inductive proximity switch. The pick-up lugs
are tapped into the shaft coupling at 180 degrees apart and rotates at the
same RPM as the motor shaft. Therefore each revolution of the motor shaft
produces two pulses on the inductive proximity switch. This signal is
monitored by a Keithley CTM05 counter card in the PC. The CTM05 counts pulses
per second, calculates turret shaft speed based on the gear ratio, and then
determines the delivered volumetric flow.
Experimental
Methods
A series of calibration test were conducted on the Yield
Monitor Test Facility system. Since this system is intended to access the
accuracy of clean grain elevator yield monitors it must first be calibrated
and validated to insure that the results that it measures are accurate. All
calibration test reported in this document were conducted using corn at normal
storage moisture content conditions.
Receiving Tank
Weigh Scale System
The load cells and transmitters were individually
calibrated in the laboratory. It was also necessary to calibrate the overall
system as installed under the receiving tank. In order to do this, the DAS801
was used to collect a tare weight from the empty receiving tank. Grain was
then transported on a flat bed fifth wheel trailer equipped with two 6.5 m3
hoppers. Approximately 5.3 m3 of grain were taken to a local feed
mill to establish a net grain weight. The batch of grain was then loaded into
the receiving tank and the batch weight was recorded using the DAS801. A
second batch was also taken to the feed mill consisting of approximately 10.6
m3 and weighed. This
method provided a reference weight for two batches independent of each other.
As a result, a response curve for 5.3 and 10.6 m3 of grain was
generated to confirm system calibration. The percentage difference between the
mill scale and the receiving tank scale for the two test batches were 0.7% for
the 5.3 m3 batch and 1% for the 10.6 m3 batch. These
percent errors were considered to be reasonable for this type of system.
Grain Meter Speed and Volumetric Delivery
The grain meter consist of two turrets, one 46 cm long
(M1) and the other 91 cm long (M2). The two meters are operated separately,
the first providing grain flow from 1.8 to 15.9 m3/hr and the
second providing flow rates from 15.9 to 159 m3/hr. The primary
strategy for calibrating the metering system was to: 1) confirm that the grain
meter level control and 30 cm supply auger are maintaining level throughout
the flow rate range and 2) determine the amount of grain moved through the
meter to the weight scale at a preset flow rate and flow duration time. This
was accomplished by selecting three discrete flow rates for M1 and six flow
rates for M2. The total grain mass and bulk density of the grain was
pre-determined and grain was circulated once through the system to ensure that
all trap points were full. The grain batch was then transferred from the
supply tank to the receiving tank with the meter running at the prescribed
flow rates. The time was recorded for complete transfer, the DAS801 was used
to record accumulated grain mass at one second intervals and the meter shaft
speed was recorded. In addition, a visual check was performed to make sure
that the minimum grain level was maintained above each turret during the
entire process. This data made it possible to determine both instantaneous and
overall variability in flow rate and shaft speed. This procedure was repeated
for all flow set points for both M1 and M2. This information was then used to
develop a linear flow set point adjustment relationship that would compensate
for error and provide an actual flow with in 0.2% of set point at corn flows
of 21.1 kg/s and 1.28% at corn flows of 1.3 kg/s. The meter shaft speeds over
the flow range from 1.3 kg/s to 21.1 kg/s were found to be fairly stable with
a mean of 636 rpm and a standard deviation of 12.1 rpm and mean of 1096 rpm
and standard deviation of 15.1 rpm, respectively. It should be noted that in
every observed case, the measured rpm varied between two points. For example,
the measured turret speed for 21.1 kg/s flow oscillated between 1080 and 1110
rpm. This is likely due to the sampling rate of 1 hz being too low. A higher
sampling rate should correct this and improve the accuracy of this
measurement.
Transport
Delays
As a result of the transport distance which exist between
the elevator and the receiving tank, it is necessary to establish a
relationship between the time at which the grain leaves the clean grain
elevator and the time at which it enters the receiving tank. The grain
transport system which is down stream from the clean grain elevator runs at a
constant speed. Consequently, for most higher grain flow rates, the transport
time should be fairly independent of the inflow rate to the elevator.
However, at the lower flow rates there may be some internal surging as the
grain builds up in the inclined section of the U-trough auger and vertical leg
of the grain pump. In order to identify these relationships a series of test
were conducted at discrete flow rates between 1.8 and 159 m3/hr. During each test the grain flow was
started at the meter with the rest of the system running. The elapsed time
required for grain to arrive at the GreenStar sensor and at the receiving tank
weight scale were documented for the range of grain flows. The results of the
transport delay test are presented in table 2.
Static Grain
Flow Tests
The major impetus of the design of this test facility was
to determine the response of the yield monitor sensor to variation in inflow
rates. Grain meter calibration tests were conducted prior to evaluating the
response of a GreenStar® yield monitor. Yield monitor data were collected
simultaneously with some of the
calibration testing. If a calibration test failed, it was repeated after data
analysis to complete all execution runs defined for the yield monitor inflow
rate test. In general, recirculation of 10.6
m3 batch of grain was limited to seven runs. There does not appear
to be any effect on the yield monitor performance as a result of the number of
grain flow cycles, with in the range of cycles used in this test. A list of
the static flow test runs are provided in Table 1.
The GreenStar® yield monitor system was equipped with
the latest hardware and firmware version presently being marketed by John
Deere as of June 2000. Likewise, the system was calibrated using the revised
two point calibration. First the system was calibrated at a corn flow set
point of 12.7 kg/s, and the recommended adjustments were made in the
calibration factor. Then the system was set to “Low Flow Comp Mode” and
the system was run at 6.3 kg/s and the flow comp number was adjusted. The
remainder of the tests were run with this calibration.
An individual static flow test was run in the following
manner. First, the test corn was transferred from the grain transport trailer
into the supply tank. Samples of grain were taken at discrete times in the
grain flow for use in an Dickey John GAC 2100 grain test unit to determine
moisture content. The bulk density and broken corn and foreign material were
evaluated using the recommended practice found in the USDA Grain Inspection
Handbook. A small sample of grain was run through the system to fill all void
spaces in the flow path from the supply tank to the receiving tank. The
SLC-500 grain meter parameters were selected to set the mode of operation and
the desired throughput. Data logging with the GreenStar® system was initiated
and a new test farm and field number were defined. The system was started up
working backward from the grain pump to the supply elevator. The grain meter
was filled with grain. Consequently, starting the grain meter and supply auger
would begin the flow of grain at the prescribed flow rate. Data was collected
for a predetermined test run time which was based on the number of bushels in
the system and the flow rate. Activating grain flow at the meter initiated
data acquisition at the weigh scale, grain meter shaft speed sensor and the
GreenStar® system. The grain flow continued until the preset runtime expired.
The system was then systematically shut down to allow all grain to move from
the grain meter through the clean grain elevator and on to the receiving tank
weight scale. The accumulated data was then saved to file on the hard drive of
the PC and the PC Card of the GreenStar® system. This data was then used to evaluate the performance of the
GreenStar® sensor under variation in inflow rate.
Results
and Discussion
The GreenStar® yield monitor sensor was evaluated for
variation in measured flow ranging from 1.3 kg/s to 21.1 kg/s. It was found
that the GreenStar® yield sensor performed well across this wide range of
static flows as shown in Table 1. At calibration
flow rates of 12.7 kg/s, the percent difference in total mass flow between the
GreenStar® and the weight scale were below 1%, while the difference only
increased to 3% at the extreme flow rates of 1.3 and 21.1 kg/s. These results
were replicated during the second set of test runs confirming that the
GreenStar® sensor is able to predict accumulated grain flow. This is further
confirmed when examining Figures 6, 7
and 8, which compare the accumulated mass of the
weight scale, GreenStar® and grain meter. At grain flows of 4.2, 12.7 and
21.1 kg/s, there is minimal observed deviation between the accumulated masses
measured and/or predicted by the three devices. In all three cases, the weigh
scale runs slightly higher than the grain meter during flow, but seems to home
in on the meter value at the end of flow. This may be caused by momentum
forces in the falling grain stream as it impacts the surface of the grain in
the weigh tank and thus transmits a dynamic load into the load cells
The GreenStar® seems to more closely follow the weigh scale at the
lower flows, while it more closely follows the meter’s accumulated mass at
the high flow rate. However, the difference is still minimal when looking at
the accumulated mass.
The
instantaneous flow rates recorded by GreenStar® exhibited a moderate amount
of variability at the calibration flow level of 12.7 kg/s, while higher
variation is experienced at the low flow rates. The instantaneous flow rates
are presented in Table 2. The mean GreenStar®
instantaneous flow rate was 13.0 kg with a standard deviation of 0.5kg. At two
standard deviations from mean the variation is under 8%. Similar results were
found for the high end flow of 21.1 kg/s. At this level, the instantaneous
flow variation is under 7%. However, the variability in instantaneous flow
becomes high at low flow rates. It is not possible to draw a firm conclusion
on the cause of variation at the
low flow rates. It could be attributed to sensor error, or it could be the
result of actual grain flow variability caused by surging within the material
handling system, or perhaps within the clean grain elevator. However, the
variability is a moderate 7% at high flow rate of 21.1 kg/s where it is not as
likely to experience flow surging. It is clear that the instantaneous flow is
not as stable across the full range of flow rates as the accumulated mass.
This is for obvious reasons, when assuming a normal distribution for all flow
conditions, the instantaneous flow variation tends to cancel each other out
and leave an accumulated mass which is a function of the mean flow rate. As
seen in Table 2, the mean flow rates of the three
devices are very similar. Another interesting observation is that
instantaneous flow rate standard deviation seems to be smaller near the
calibration points and increases at the extreme flow rates. Although the
GreenStar® sensor appears to do a good job of predicting total accumulated
mass flow at the extremes flow rates, the instantaneous flow rates may be less
reliable further away from the calibration point.
The variation in instantaneous flow rates at the meter
are minimal, as shown in Table 2. This is to be
expected, since the turret rpm is fairly stable. However, the higher variation
in instantaneous flow of the weigh scale is somewhat to be expected. The
hysteresis of the load cells is 0.02% of the full scale load of 4536 kg, which
is 0.9 kg of potential load variation. On a per second flow basis this can be
significant at low flows. Another potential source of variation in the weigh
scale may be vibration from the grain pump. Although slip joints were provided
to isolate the weigh scale tank from the grain pump, there appears to be some
vibration transmitted by friction in these joints. Another potential cause of
variation may be momentum force loading from the falling grain stream. It was
found that the use of a running average filter, helps minimize the influence
of these dynamics. The data presented in Table 1 and
Figures 6, 7, and 8
are un-filtered accumulated flow values. However, the data presented in Table
2 for the weigh scales are instantaneous one second flows filtered with a
five second averaging filter.
However, it should be remember that most flow experienced
by an actual combine yield monitor system will be in the range of 4.2 and 16.9
kg/s. Consequently, the main issue to consider is whether an instantaneous
flow rate variation of approximately 7% is acceptable at calibration flow
levels. More importantly, is the sensed flow variation caused by the mass flow
technique or the yield monitor, or are these flow variations an artifact of
the grain metering and transport components of the test facility.
Summary
and Conclusions
Performance results of the Yield Monitor Test Facility
were positive, although a few limitation have been identified. First, it was
found that the grain metering system can accurately meter grain at varying
flows to the clean grain elevator with excellent accuracy over a prescribed
period of time. A potential concern is whether or not the grain flow to the
GreenStar® sensor is instantaneously uniform, or are there flow ripples due
to the grain handling system. Secondly, the weigh scale system appears to be
very accurate in measuring the accumulated mass flow in the system. However,
the potential for grain stream dynamics, tank vibration and load cell
hysteresis confound attempts to measure instantaneous grain flow at small flow
rates ( 1 to 2 kg/s). Thirdly, the GreenStar® sensor demonstrated high
accuracy across a range of static flow rates ranging from 1.3 to 21.1 kg/s.
When considering accumulated mass flow, the percent difference between
GreenStar® and the weigh scale were less then 1% at calibration flow rates
and approximately 3% for extreme flow rates. However, the accuracy of
GreenStar® instantaneous grain flow is somewhat suspect. Variations in
instantaneous one second grain flows were observed to be approximately 8% at
calibration flow rates.
Although the results from these test indicate that the
GreenStar® mass flow sensor accurately predicts total accumulated mass flow
across a broad range of static inflow rates, one must consider the possibility
that other sources of error may exist in the overall combine yield monitor
system. For instance; error in ground speed, measured swath width, transport
delays in the threshing unit and other issues may still influence the overall
accuracy of the yield map.
Acknowledgments
The authors would like to extend their grateful
appreciation to Ed Hutchens, Carl King, Lee Rechtin, and Ed Roberts for there
help fabricating, assembling the system components, and transporting the
grain, to Lloyd Dunn and Burl Fannin for there help in wiring the controls and
instrumentation, to John Deere Corporation, Hutchinson, and White Hydraulics
for technical and equipment support and to Mike Ellis of the Worth and Dee
Ellis Farms for providing grain for the test.
References
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