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Monitoring the Controlled Atmosphere Storage Environment: Ammonia Sensors and Infrared Vapor AnalysisJeff Griffin, Pete Eschbach, and Josh Poulson(1) and Nate Reed(2) (1)Battelle Northwest Laboratories 16th Annual Postharvest Conference, Yakima, WA |
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This presentation summarizes the results of experimental work performed over the past two years under funding by the Washington Tree Fruit Research Commission (WTFRC). Objectives of this effort have been: 1) identification of reliable ammonia sensors suitable for detection of refrigerant leakage in controlled atmosphere (CA) rooms, 2) quantification of ammonia loss due to water uptake in room-sampling lines, 3) development of a new demand-defrost sensor for CA refrigeration systems to improve energy efficiency, and 4) an evaluation of the use of infrared analysis methods (specifically Fourier-transform infrared spectroscopy or FTIR) for continuous monitoring of ethylene, water vapor, and other vapors (especially flavor-related esters and aldehydes) in the CA environment. | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Evaluation of Ammonia Sensors
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The experimental setup for ammonia sensor evaluations appears in Figure 1. This system is installed at the Stemilt Growers CA storage facilities in Wenatchee, WA and has been in operation for nearly two full storage seasons (November 1998 through July 1999 and November 1999 through May 2000). Airflow for all sensors is drawn from fruit-filled CA rooms to a common sampling manifold. The 40 rooms are sequentially sampled for a 5-minute period at a nominal flow rate of 6 L/min. Following the oxygen and carbon dioxide monitors, CA room vapors enter the ammonia sensor testing section where computer-controlled injections of 10 to 15 ppmV of ammonia are made hourly. The flow is then divided amongst the ammonia sensors under test. Flow rate to each sensor is set per manufacturer's specifications using individual rotameters. Sensors evaluated during the past two storage seasons are summarized in Table 1. Table 2 summarizes the results of the ammonia sensor evaluation study to date. Figure 1. Ammonia sensor testing system.
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Performance of Individual Ammonia Sensors
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All sensors were exposed to hourly, 5-minute injections of ammonia at the 10- to 15-ppmV level. Dilution air was supplied from the Stemilt CA rooms. An "optimum" sensor response consisted of 24 signal output spikes (one per hour for 24 hours) with no output or baseline drift between injections. For these evaluations, in addition to sensor outputs, a number of ancillary variables were monitored, including: 1) voltage to the ammonia injection solenoid, 2) carbon dioxide concentration, 3) oxygen concentration, 4) CA room number, and 5) relative humidities at the input and exhaust of the sensor testing system. David Bishop Model 730 Figure 2. Response of David Bishop ammonia sensor.
Sensidyne Model 1000 EIT "Sensor Stik" MST Model FMS 8710 with Model 9602-6700 Sensor Module Figure 3. Response of MST ammonia sensor.
BW Technologies "Plant Rat" Figure 4. Response of BW Technologies "Plant Rat" ammonia sensor.
Draeger Polytron 2 Figure 5. Response of Draeger ammonia sensor.
NexGen Ammonia Detector Figure 6. Response of NexGen ammonia sensor.
Pacific Technologies (alarm type) Figure 7. Response of Pacific Technologies alarm-type ammonia sensor.
Pacific Technologies (analog type) Figure 8. Response of Pacific Technologies analog-type ammonia sensor.
Industrial Scientific Figure 9. Response of Industrial Scientific ammonia sensor.
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Summary of Ammonia Sensor Evaluations
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By the end of this storage season (August 2000), we will have evaluated eight different electrochemical ammonia sensors (David Bishop, Sensidyne, EIT Sensor Stik, MST, BW "Plant Rat", Draeger, US Industrial, Inmet). To date, the performance data indicate:
By the end of this storage season, we will have also evaluated three different optical ammonia sensors (NexGen, Pacific Technologies, Industrial Scientific). To date, the data indicate:
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Demonstration of Ammonia Uptake in Sampling Lines
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In fall 1999 we performed laboratory experiments at Battelle facilities in Richland, WA to demonstrate and quantify uptake of ammonia in CA room sampling lines. The laboratory evaluation system is depicted schematically in Figure 10. Figure 10. Laboratory setup for ammonia uptake studies.
To conduct these investigations, 200 feet of 1/4-inch ID TygonTM tubing (provided by Nate Reed, Stemilt Growers) was enclosed in an environmental chamber where temperature could be lowered below the dewpoint to induce condensate formation in the tubing. Moist air (70% RH) and dilute ammonia vapor (55 ppmV) were introduced at the tubing input and the chamber temperature was lowered until condensate formation began. A plot of the experimental data appears in Figure 11. Figure 11. Experimental data indicating ammonia uptake by water in sampling lines.
Ammonia concentration at the tubing exhaust was observed to drop to 15 ppmV (from the original 55 ppmV) due to the presence of liquid water in the tubing. Note that most commercial ammonia sensors have a low detection limit of a few ppmV of ammonia. Consequently, if our injected ammonia concentration had been lower (say 10 to 15 ppm) the ammonia level at the tubing exhaust could have gone undetected by any existing commercial ammonia sensor. Therefore, the data suggest:
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Infrared Vapor Analysis in CA Rooms
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In the original sensor suited installed at Stemilt Growers for ammonia sensor evaluation, a MIDAC FTIR system was utilized in the exhaust line to verify ammonia concentration. During the current storage year (November 1999 through August 2000) this infrared analyzer has been utilized to monitor ethylene and other vapors coming from the CA rooms. Representative ethylene concentration data for the Stemilt CA rooms appear in Figure 12 and 13. Figure 12. Ethylene concentration for single CA room for two-week period in 2000.
Figure 13. Single-day ethylene concentration for all 40 Stemilt CA rooms (room number "0" indicates hallway measurement).
The Midac FTIR vapor analysis system can also be used to monitor "flavor vapors" in apples and other fruit. The feasibility of monitoring butyl acetate was demonstrated in a laboratory experiment performed at PNNL facilities in Richland. Resulting data are displayed in Figure 14. Figure 14. Detection of butyl acetate in Red Delicious apples.
Finally, the feasibility of monitoring 1-methylcyclopropene (MCP), a ripening inhibitor, was demonstrated using the Midac instrument at Stemilt facilities in Wenatchee, WA. Representative data appear in Figure 15. Figure 15. Infrared absorption spectrum for methylcyclopropene (MCP).
The use of FTIR instrumentation for continuous, real-time analysis of CA room vapors appears entirely feasible. While the instrumentation is fairly expensive ($35,000 to $40,000), the method allows a level of continuous room monitoring which heretofore was not possible (e.g., the measurement of ethylene in CA rooms is typically performed by bagging gas samples and analyzing them in an offsite gas chromatography laboratory). In addition, a single FTIR system can simultaneously monitor a wide variety of CA room vapors including ethylene, ammonia, and butyl acetate (from Red Delicious), as well as other "flavor" gases that affect fruit quality. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Article # PC2000FF
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