Ammonia Absorption in Room Temperature Ionic Liquids
Ionic liquids are relatively new generation solvents with low vapor pressure and high thermal stability. The solvency of the ionic liquids can be tuned by the variation in ion types, substitution and composition to provide unique properties to many industrial applications. In our research group, we have over 100 ionic liquids in our library.
Ammonia water vapor absorption system is an ancient heating/cooling system for large industrial applications. The physical properties of ammonia provide efficient, low cost cooling for large systems. The major drawback of the current system is the high cost of separation of water and ammonia in a separation unit. Ionic liquids with low vapor pressure offer an opportunity to overcome this problem and lower the operation costs. Our research group’s goal is to utilize ionic liquids to provide a high efficiency and economic alternative to the current system.
Explosion Suppression of Metal Dust Deflagrations
Driven by increased industry mandates for process safety, explosion protection via active suppression has expanded significantly as an effective means of restraining the maximum explosion pressure below the design pressure of the process vessel (such that catastrophic damage does not occur). During a contained deflagration event, a standard suppression design operates as follows: Upon ignition of the process media, the contained combustion begins to develop pressure. In response to detection of this pressure wave, sufficient suppressant agent is dispersed into the protected volume, absorbing the heat away from the flame front and limiting pressure rise.
In comparison to standard organic process media, metallic dusts present non-standard, highly reactive situations due to their higher rates of pressure rise (Kst), higher heats of combustion, and radiative deflagration propagation properties. In collaboration with Fike Corporation, the Shiflett group aims to characterize a more efficient inhibitor for contained metal dust combustion suppression designs. During Phase I of this study, the thermal stability and effective heat absorpotion of various inhibitor candidates are to be measured via Thermogravimetric Analysis and Differential Scanning Calorimetry, respectively. Phase II of the project is composed of particle size distribution analysis and large-scale suppression testing, to be performed in the one cubic meter test sphere located at Fike Corporation. The ensuing pressure profile would act as a direct indicator of the effectiveness of the inhibitor, with a limited total suppressed pressure (TSP) corresponding to the practicality of an agent towards industry application.
The results yielded from this research offer a thorough investigation into an optimized inhibition agent for the explosion suppression of metal dust induced deflagrations and provide customers with a cost effective explosion protection solution for highly energetic metallic combustion fuels.
Sulfite Removal from Wine
Within the winemaking industry, sulfites are used as a chemical additive to prevent wines from spoiling or browning as they age, and to ensure that wines are free of unwanted bacteria at the time of opening. While there are obvious advantages to using sulfites in wine, a small percentage of the population experiences severe adverse health effects as a result of a sulfite sensitivity. These people may experience asthma attacks, rashes, and headaches as a results of the presence of sulfite in wine. Our research group is designing a device to go on the end of a wine bottle to remove sulfites from wine at the time of pouring. Students are working to design and print a 3D prototype, while also investigating materials such as zeolites, ion exchange resins, and clays to discover which materials may selectively remove sulfite without changing the taste of wine. Students are using a combination of qualitative and quantitative techniques to investigate which materials may be more successful at removing sulfites than the few commercial products that already exist on the market. It is the hope of our group to design a cost-effective single use device to allow wine drinkers to enjoy wine without the presence of unnecessary chemical additives.
Creating Cold-Chain Independent Vaccines with Inorganic Vehicles
The refrigeration of vaccine is critical to maintaining their efficacy. Vaccines are mainly composed of proteins, most of which are very sensitive to temperature changes. The cold chain cycle assures that vaccines are stored in controlled environments, between 2 to 8°C, to avoid conformational changes in protein structures. Keeping a constant environment that is optimal to the vaccine reduces changes to the protein’s secondary and tertiary structures while maintaining the vaccine’s potency. Any deviation from this range can result in significant waste and lead vaccination programs to a deficit. This is a common concern especially in developing countries where access to the necessary resources to store vaccines and a constant source of electricity are limited.
In the Shiflett group, we are currently trying to eliminate a vaccine’s dependency on refrigeration to reduce waste, cost, and increase the access of vaccines to those who need them. To accomplish this, we are currently working with Dr. David Corbin (Senior Scientist, CEBC) and Dr. William Picking (Distinguished Professor, KU) on selecting and developing vaccine specific inorganic vehicles that will act as thermal stabilizers and enhancers due to their adjuvant properties. Dr. William Picking, an expert in vaccines and pathogenic microbiology, completes our team by integrating his knowledge of pathogens, as we work to characterize the interactions between the inorganic vehicles and the Invasion Plasmid Antigen D. Together we are looking to apply our knowledge and resources to thermally stabilize vaccines in tailored inorganic materials.
Removal of PFOA from Drinking Water Using Microporous Zeolites
Local, state, and federal governments are responding to perfluoroalkyl substances (PFAS) that are being detected in drinking water. These persistent materials are bioaccumulative and maybe linked to human and animal health problems. The State of New Jersey recently set the first drinking water standard in the U.S. for perfluorononanoic acid (PFNA) at 13 parts per trillion (ppt) which is only one of many known PFAS. Other common PFAS include perfluorooctanoic acid (PFOA) and perfluorooctanoic sulfate (PFOS). PFAO has been used in the production of a variety of materials such as nonstick Teflon™ cookware, firefighting foam and water repellant coatings. Recently, high levels of PFOA and PFOS were detected in the drinking water in Parchment, Michigan. The state’s Department of Environmental Quality (DEQ) results showed water with 1,410 ppt (740 ppt PFOS and 670 ppt PFOA). Michigan in January adopted 70 ppt as a legally enforceable level for PFOS or PFOA in drinking water. Today, almost every week a new story about drinking water contaminated with PFAS is appearing in the news. The U.S. Environmental Protection Agency (EPA) is recommending that drinking water should contain less than 70 ng/L (70 ppt) of PFOA. The Shiflett group is studying a variety of materials for removing PFOA, PFOS, and other PFAS compounds from drinking water. They have recently discovered a family of zeolites that can remove PFOA from aqueous solutions that may be more cost effective than activated carbons. Along with the removal of PFOA from drinking water, the team is working with the Department of Chemistry to develop an ultra-performance liquid chromatography (UPLC) triple quad mass spectrometer (MS) technique (UPLC-MS) for detection of PFOA and other PFAS materials below 10 ppt.
Designing Molecular Gate Adsorbents for Natural Gas Purification using PSA
The PSA system is used to study the separation of contaminants such as N2, CO2, CO, and H2S from natural gas (NG). Shiflett lab group is currently working with Dr. David Corbin (Senior Scientist, CEBC) to develop new molecular sieves for the kinetic separation of N2, CO2, CO, and H2S from NG.
To remove contaminants, the natural gas is fed under pressure through a PSA column containing molecular sieve which can adsorb N2, CO2, CO, and H2S. After the sieve is saturated with N2, CO2, CO, or H2S, the flow is redirected to the next column and the first column is depressurized to desorb the N2, CO2, CO, and H2S and regenerate the sieve. In some cases the desorption is slower than the adsorption step, so multiple columns are needed to allow time for complete column regeneration. Development of a molecular sieve to remove N2, CO2, CO, and H2S from CH4 based on size difference is challenging because they only differ in size by 0.2 Angstroms (N2, CO2, CO, and H2S are about 3.4 to 3.6 Angstroms vs. CH4 is 3.8 Angstroms). However, if a molecular sieve can be developed for this application, it will significantly reduce the cost of separating inert gases such as N2, CO2, CO, and H2S and possibly He from NG. Current technologies, such as cryogenic plants for N2 removal, are complex and have high capital and operating costs compared to using a PSA system. The PSA technology is also field deployable, modular and can be scaled out to meet the capacity of the gas field.
Water Desalination via Gas Hydrate Technology
Global population continues to increase, consequently the demand for freshwater keeps rising. As a response to this pressing need, several desalination plants have developed during the past decades. Most of these utilize reverse osmosis (RO) or multi-stage flash distillation (MSF) as their separation technology. However, pumping large amounts of liquids to elevated pressures and the significant thermal heating requirement makes these technologies expensive. An alternative desalination technology is the use of clathrate hydrates.
A clathrate hydrate is a crystalline cage-like water structure which encloses a guest molecule. The conditions at which clathrate hydrates form are specific to the guest molecule. In past experiments, researchers have investigated several different refrigerants (HCFC-22, HFC-134A, HCFC-141b, etc.) as clathrate formers to separate brine from freshwater and have observed clathrates form at temperatures above the freezing point of water. This is an important benefit because it decreases the energy needed to cool the seawater to reach crystallization conditions. Nonetheless, due to the ozone depletion and global warming potentials related to CFCs, HFCs, and HCFCs, the clathrate formers investigated in the past are no longer environmentally viable.
The purpose of our research is to identify an optimum clathrate former. We will achieve our goal through fundamental studies on phase transition properties, hydrate formation kinetics, and solubility of refrigerants in saline water, while simultaneously sustaining a pragmatic approach to desalinating water by considering heat integration and technology coupling.