Source: ELTRON RESEARCH INCORPORATED submitted to
REGENERABLE ETHYLENE REMOVAL
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
EXTENDED
Funding Source
Reporting Frequency
Annual
Accession No.
0222877
Grant No.
2010-33610-21490
Project No.
COLK-2010-02161
Proposal No.
2010-02161
Multistate No.
(N/A)
Program Code
8.13
Project Start Date
Sep 1, 2010
Project End Date
Aug 31, 2013
Grant Year
2010
Project Director
Schutte, E. J.
Recipient Organization
ELTRON RESEARCH INCORPORATED
4600 NAUTILUS COURT SOUTH
BOULDER,CO 80301
Performing Department
(N/A)
Non Technical Summary
Fresh fruit, vegetables, and flowers are transported and stored in refrigerated containers. As the produce ripens, ethylene gas is produced, which further ripens the product and can lead to premature spoilage. Most fruits and vegetables emit ethylene gas which promotes ripening. Certain species, such as apples and bananas, produce more ethylene than others. Elevated ethylene levels can significantly reduce storage time; concentrations as high as only 1 ppm can destroy an entire container of produce in one day. The current ethylene removal industry uses single-use potassium permanganate adsorbent blankets or sachets, or a removal device that has a limited lifetime (38 months). Other devices that are on the market or currently being developed include biofilters, ozone generators, and photocatalytic and electrocatalytic devices. Disadvantages of these devices include very strict storage requirements, the potential of contamination by the ethylene-destroying bacteria, the need to employ complex systems to produce ozone, and high manufacturing costs of the photocatalytic device and nanoporous gold electrocatalysts. The goal of this Phase II program is to optimize the adsorbent, complete the design and fabricate a bench top, multi-bed unit. The research will be focused on long-term testing (months instead of days), extended testing under high humidity conditions, testing at concentrations below 1 ppm, testing mold spore kill efficacy of the adsorbent, and evaluation in atmospheres with fluctuating concentrations of ethylene. Engineers at Eltron will be called upon to finalize the design and subsequently build the multi-fixed bed system, which is optimized towards our primary adsorbent and the optimal conditions found during the research. Major benefits of the new system include the ability to regenerate the adsorbent (long lifetimes without having to replace the active species), use of relatively inexpensive materials (no platinum, ruthenium, or gold), and a simple device design, making it inexpensive to manufacture and simple to use. The low maintenance design of the device will allow for increased storage time and reduce spoilage, resulting in reduced costs to all parties along the supply chain - grower, transporter, distributor, and consumer. A renewable ethylene adsorption system would be able to reduce ethylene concentrations within refrigerated dock-side storage containers, refrigerated train cars and grocery store storage refrigerators at minimal long-term cost, and would eliminate the cost and hassle of frequently changing disposable adsorbent beds. By the end of the Phase II program, a prototype low-cost device for the removal of low concentrations of ethylene will have been fabricated, evaluated in a lab setting and in a real-world setting by Ethylene Control Inc., who has already expressed interest in this technology. During Phase II, partnerships for the commercialization of the device will be initiated in order to bring the product to market as soon as possible.
Animal Health Component
(N/A)
Research Effort Categories
Basic
(N/A)
Applied
100%
Developmental
(N/A)
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
5031199202040%
5031199200060%
Goals / Objectives
During Phase I, Eltron developed regenerable adsorbents for ethylene removal and finished preliminary designs of a prototype ethylene removal device. Data collected during the Phase I showed that Eltron's primary adsorbent was capable of removing 100% of the ethylene in a 5 ppm ethylene/air stream for over 24 hours in dry conditions and for 2.5 hours in humid (60% relative humidity) conditions. The adsorbent was shown to be regenerable in both dry and humid conditions through multiple cycles with no substantial loss in activity. The specific objectives for Phase II are as follows: 1) Construct multiple bench-scale reactors, one for short-term/kinetic testing and one for long-term cyclical testing, 2) Scale-up synthesis of downselected adsorbent from Phase I; characterize and test to ensure large scale synthesis does not compromise activity of adsorbent, 3) Perform more in-depth examination of various pelletization and binding techniques and their affect on adsorbent activity in both short- and long-term tests, 4) Test mold spore kill efficacy of regenerable adsorbent, 5) Determine effects of long-term (months) exposure of primary adsorbent to humidified ethylene/air streams, 6) Determine optimal adsorption/regeneration cycle times for adsorbent, 7) Determine the effect gradual ethylene concentration changes have on adsorbent activity over long-term cyclical runs, 8) Use kinetic and long-term data to complete final design of multi-fixed bed, scaled-up reactor system, 9) Fabricate multi-fixed bed reactor system, 10) Run initial tests on scaled-up reactor system to verify effectiveness, and 11) Deliver scaled-up reactor system to Ethylene Control, Inc. or other company involved in refrigeration/transportation of perishables. Major benefits of the new system include the ability to regenerate the adsorbent (long lifetimes without having to replace the active species), use of relatively inexpensive materials (no platinum, ruthenium, or gold), and a simple device design, making it inexpensive to manufacture and simple to use. The low maintenance design of the device will allow for increased storage time and reduce spoilage, resulting in reduced costs to all parties along the supply chain - grower, transporter, distributor, and consumer. A renewable ethylene adsorption system would be able to reduce ethylene concentrations within refrigerated dock-side storage containers, refrigerated train cars and grocery store storage refrigerators at minimal long-term cost, and would eliminate the cost and hassle of frequently changing disposable adsorbent beds. By the end of the Phase II program, a prototype low-cost device for the removal of low concentrations of ethylene will have been fabricated, evaluated in a lab setting and in a real-world setting by Ethylene Control Inc., who has already expressed interest in this technology. During Phase II, partnerships for the commercialization of the device will be initiated in order to bring the product to market as soon as possible.
Project Methods
The approach for this Phase II program will be focused on long-term testing (months instead of days), extended testing under high humidity conditions, testing at concentrations below 1 ppm, testing mold spore kill efficacy of the adsorbent, and testing in atmospheres with fluctuating concentrations of ethylene. Engineers at Eltron will be called upon to finalize the design and subsequently build the multi-fixed bed system, which has been optimized towards our primary adsorbent and the optimal conditions found during the research. During the Phase II program, partnerships for the commercialization of the device will be initiated with the goal of bringing the product to market within five years. Regenerable adsorbents will continue to be prepared using standard methods such as co-precipitation, ion-exchange, and/or impregnation. Physical characterization will be performed on the adsorbents using established analytical techniques including but not limited to: SEM/EDX; XRD; and surface area and pore size analysis. The adsorbents will be evaluated for ethylene removal and regeneration using a pair of custom made fixed bed reactors fitted with humidity sensors and which are capable of operating between -10 oC and 120 oC. One reactor will be used for long-term testing while the other for short term and regeneration cycle optimization studies. All adsorbent testing, including regeneration cycle optimization tests, will be run utilizing low concentrations of ethylene in humidified air during adsorption half-cycles and room temperature or heated air during desorption half-cycles. Gas chromatography will be used to determine removal rates. The long-term reactor will be fitted with an auto-sampling system so inlet and outlet streams can be sampled and evaluated 24 hours a day, seven days a week. All adsorbents will be sent to laboratories specializing in mold spore kill efficacy studies to determine the effectiveness of Eltron's primary sorbent in eliminating this other risk to fresh produce. The effectiveness of the sorbents to handle changes in ethylene concentration over time will also be examined utilizing a pre-reactor cylinder filled with a specified amount of ethylene which is then gradually released and fed to the bed using a constant air flow. Attrition resistance studies will also be performed on optimized adsorbents synthesized with various binders. Kinetic studies will be performed on down selected adsorbent(s) and a prototype, multi-fixed bed reactor system will be designed and built based on this data, tested initially at Eltron and then scaled-up for testing in a real-world environment at a company involved in refrigeration/transportation of perishables.

Progress 09/01/11 to 08/31/12

Outputs
OUTPUTS: During the previous year we completed long term tests on the primary adsorbent as well as ZSM5 to determine adsorptive capacities for ethylene and water respectively. We also completed automation upgrades on the reactor system and also upgraded our humidity sensors to a pair that work at higher pressures. New Teflon containing adsorbent derivatives were also synthesized and tested. Tests were also run to help determine lifetime of adsorbent, to help determine if fluctuations in ethylene concentration over time would affect the performance of the adsorbent, and to determine how efficient our adsorbent was at removing ethylene at concentrations below 1ppm. We also laid initial engineering groundwork and completed a design for a medium sized ethylene removal prototype to be built over the remaining stages of the no-cost extension. A 10 fold scale up of the synthesis of our primary adsorbent was also performed. PARTICIPANTS: Erick Schutte, Ph.D. has been the primary researcher on this project. Dr. Schutte has extensive experience with heterogeneous catalysts and adsorbents and has participated in over 10 projects at Eltron, during his nine years with the company, which were directly focused on the research and development of catalysts and adsorbents. Jim Fisher is an engineer at Eltron Research and Development who has performed the initial engineering work and design on the prototype system to be built over the remaining months of the project. During his seven years with the company Mr. Fisher has prepared preliminary economic viability estimates for several processes under research and development and contributed his experience and expertise in the design and construction of many bench and floor scale experimental research setups. Allan Klinge, Sales and Marketing director of Klinge Corporation was contacted during this reporting period. Klinge Corporation is the world's leading manufacturer of refrigerated transport containers. TARGET AUDIENCES: Allan Klinge of Klinge Corporation, a company specializing in the design and manufacture of refrigerated shipping containers, was contacted in an effort to gauge industry interest. Mr. Klinge was very helpful in revealing how the refrigerated container industry works, what the key drivers are, and most importantly that we may want to focus on designing a system of this type to be used in warehouses and storage facilities as those are easier markets to get in to and have greater pain in the area of ethylene abatement. PROJECT MODIFICATIONS: The only major change during this reporting period was our decision to change our focus from designing a system for refrigerated shipping containers to design a system to remove ethylene from refrigerated storage areas and warehouses. These changes were made based on us getting a better understanding of the steps already being taken to remove ethylene on board large transport ships which include 60 to 80 air exchanges an hour. Additionally, it was discovered that the shipping industry is not particularly interested in modifying shipping containers unless the customer pushes them to do so and based on our conversations with people within the refrigerated shipping industry there is not a great deal of concern by customers in regards to ethylene removal. However, ethylene build up within refrigerated storage facilities and warehouses is an area where the customer is concerned and the immense energy requirements of exchanging air in these facilities is not economically viable so solutions are being asked for and identified.

Impacts
Two new adsorbent variants synthesized using colloidal Teflon were produced in an attempt to make the current base adsorbent more hydrophobic. It was hoped that an adsorbent could be produced which would repel the polar water molecule while still retaining the ability to bond ethylene. Unfortunately the changes only appeared to block silver bonding sites leading to quicker ethylene saturation times for the adsorbents with little to no effect on the uptake of humidity. In addition to the variant testing we were able to upgrade and redesign our two testing reactors. The addition of two high-end humidity sensors capable of functioning at pressures above ambient and further automation of the overall system gave us the ability to run much more accurate humidity-based tests. Over the course of the second year we were able to determine the ethylene and humidity saturation levels for our base adsorbent, determined the length of time for effective regeneration for both ethylene and water containing adsorbents, and ran a series of adsorption regeneration cycles to determine stability in both dry and humid conditions. Multiple cyclical tests were also performed at very low ppm levels, below 1ppm, as current ethylene removal techniques such as potassium permanganate sachets, become less effective and efficient at levels below 1ppm. As with all of the other ethylene concentrations tested our primary adsorbent was able to consistently reduce ethylene concentrations below 30ppb, which was the lowest concentration that we could reliably detect with our current instrumentation. Regeneration of the primary adsorbent, from both ethylene and humidity saturation, was also achieved consistently over multiple cycles without any reduction in effectiveness. Furthermore, fluctuations of 4 ppm over times as long as three hours and as short as 45 minutes were shown not to affect the adsorption of ethylene until saturation was reached. We also demonstrated that our primary adsorbent could be scaled-up by a factor of 10 without there being any changes to the physical characteristics or operating performance ensuring that large scale production will not be an issue. An initial design of a prototype unit aimed at the small to mid-size refrigerated storage market was also produced and steps are now underway to produce more detailed drawings and begin the costing and construction.

Publications

  • No publications reported this period


Progress 09/01/10 to 08/31/11

Outputs
OUTPUTS: The primary goal during this first year of the Phase II program was aimed at optimizing the adsorbent on a number of fronts including saturation volume, regeneration time and efficiency, lifetime, and humidity efficiency. We successfully constructed two reactor systems, one manual and one automated each with its own separate gas chromatograph. The reactors were designed to hold the adsorbent in a quartz tube within a larger tube enabling liquid cooling of the bed to temperatures often seen in refrigerated environments. These reactors were used to run over 50 separate experiments, many which took three to four days to complete helping us acquire the data needed to accomplish the goals laid out above. PARTICIPANTS: Erick Schutte, Ph.D. has been the primary researcher on this project. Dr. Schutte has extensive experience with heterogeneous catalysts and adsorbents and has participated in over 10 projects at Eltron, during his nine years with the company, which were directly focused on the research and development of catalysts and adsorbents. Dave Biswell of Ethylene Control, Inc. in Selma, CA. was contacted prior to the start of the project. Ethylene Control manufactures many different ethylene control devices for shipping and refrigeration of fruit and produce, all of which employ potassium permanganate as the oxidizer. Charlie Ramos, the Managing Director of BioGreen Engineering LLC, Orlando FL. was engaged to help us complete a detailed Commercialization Strategy Report for our technology. TARGET AUDIENCES: Dave Biswell of Ethylene Control, a company specializing in the design and manufacture of potassium permanganate based filters, bags, and sachets, was contacted in an effort to gauge industry interest. Mr. Biswell was very helpful in revealing what the current state of the ethylene control market is, who the key players are, and what pain still exists for the various customers. Mr. Biswell also outlined the shortcomings of his products including the fact that they do not perform well once ethylene concentrations fall below 1ppm. Further discussions with Mr. Biswell are expected to take place as we continue to drive towards design and manufacture of a prototype system by the end of the Phase II. PROJECT MODIFICATIONS: Nothing significant to report during this reporting period.

Impacts
Five new adsorbent variants were synthesized, characterized and were examined in three significant test series which helped us identify a new adsorbent variant which has a higher ethylene capacity than our previously downselected adsorbent from the Phase I. This adsorbent appears to see an improvement in desorption and adsorption as it is put through multiple cycles. Testing also revealed that the ethylene bonding capacities for the adsorbents are related to both ethylene concentration and temperature. In the case of ethylene concentration changes we have found that slow changes from high to low and back to high concentration over long periods of time are mirrored by an ethylene release from the adsorbent and an increase in adsorption respectively. However, fast changes lead to offset peaks and valleys in the release and adsorption curves. Additionally, a comprehensive Commercialization Strategy Report was completed which has helped up develop a much clearer picture of markets and potential customers as well as potential setbacks and issues we must overcome in order to get our system to market. The automated reactor unit can be used with and without added humidity and is capable of being programmed to operate around the clock, cycle between adsorption and regeneration indefinitely, operate under static or changing ethylene concentrations, and operate under static or changing flow rates. The software was developed in-house so if any issues or problems arise or upgrades are needed they can be addressed immediately. We also discovered a variant of our original downselected adsorbent which has a much greater capacity for ethylene adsorption. The propensity for our adsorbents to competitively bind water was also reconfirmed during early tests and we believe we have produced a hydrophobic version of our adsorbent using colloidal Teflon. We did not have time to test this particular variant prior to this report, but we did characterize the material and successfully pelletized it. Testing also confirmed the inverse relationship between ethylene concentration and the adsorption capabilities of our adsorbents and revealed that even small concentration effects can have a substantial affect on overall performance. Finally, the confirmation that all variants take much longer to regenerate than they do to adsorb ethylene and reach saturation has helped us make early stage decisions in regards to the design and construction of the prototype system in the second year. We also worked closely with the Larta Institute and Charlie Ramos, the Managing Director of BioGreen Engineering LLC, Orlando FL, to complete a detailed Commercialization Strategy Report. The report includes barriers we identified which may hinder commercialization and potential solutions, a competitive matrix, and a commercialization roadmap. The development of the report has been incredibly important as it revealed many issues and potential problems we were not aware of related to our technology and competing technologies.

Publications

  • No publications reported this period