SUPERCRITICAL FLUID SPRAY APPLICATION PROCESS for ADHESIVES and PRIMERS SERDP Project PP-1118 Marc D. Donohue Principal Investi
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Supercritical Gel Drying of Polymeric Hydrogels for Tissue
1123 A publication of CHEMICAL ENGINEERING TRANSACTIONS The Italian Association VOL. 32, 2013 of Chemical Engineering Online at: www.aidic.it/cet Chief Editors: Sauro Pierucci, Jiří J. Klemeš Copyright © 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-23-5; ISSN 1974-9791 Supercritical Gel Drying of Polymeric Hydrogels for Tissue Engineering Applications Stefano Cardea*, Lucia Baldino, Iolanda De Marco, Paola Pisanti, Ernesto Reverchon Department of Industrial Engineering, University of Salerno, Via Ponte Don Melillo, 84084, Fisciano, Italy [email protected] Tissue engineering (TE) is an emerging field aimed at repairing defective tissues and organ, instead of relying on conventional organ transplantation. Among the polymeric materials proposed for TE applications, the water-soluble polymers have been frequently used in form of hydrogels, that are a class of highly hydrated polymer materials. Nevertheless, hydrogel materials have poor mechanical properties; as a result, this scaffolding approach is seldom used for hard tissues applications. With the aim of overcoming this limitation, drying processes have been often applied to eliminate the water from hydrogels and amply the range of applications of the water-soluble polymeric scaffolds, but these techniques present several limitations. For this reason, in this work we proposed a supercritical gel drying method coupled with a water/solvent substitution step. PVA, Alginate and Chitosan hydrogels were processed and opportunely characterized from a macroscopic and microscopic point of view. Supercritical gel drying process confirmed to be effectiveness for the formation of polymeric scaffolds; in particular, we obtained stable 3-D structures with nanometric porous morphologies suitable for TE applications. 1. Introduction Tissue engineering (TE) is an emerging field aimed at repairing defective tissues and organ, instead of relying on conventional organ transplantation. -
Supercritical Fluid Extraction of Positron-Emitting Radioisotopes from Solid Target Matrices
XA0101188 11. United States of America Supercritical Fluid Extraction of Positron-Emitting Radioisotopes From Solid Target Matrices D. Schlyer, Brookhaven National Laboratory, Chemistry Department, Upton, Bldg. 901, New York 11973-5000, USA Project Description Supercritical fluids are attractive as media for both chemical reactions, as well as process extraction since their physical properties can be manipulated by small changes in pressure and temperature near the critical point of the fluid. What is a supercritical fluid? Above a certain temperature, a vapor can no longer be liquefied regardless of pressure critical temperature - Tc supercritical fluid r«gi on solid a u & temperature Fig. 1. Phase diagram depicting regions of solid, liquid, gas and supercritical fluid behavior. The critical point is defined by a critical pressure (Pc) and critical temperature (Tc) for a particular substance. Such changes can result in drastic effects on density-dependent properties such as solubility, refractive index, dielectric constant, viscosity and diffusivity of the fluid[l,2,3]. This suggests that pressure tuning of a pure supercritical fluid may be a useful means to manipulate chemical reactions on the basis of a thermodynamic solvent effect. It also means that the solvation properties of the fluid can be precisely controlled to enable selective component extraction from a matrix. In recent years there has been a growing interest in applying supercritical fluid extraction to the selective removal of trace metals from solid samples [4-10]. Much of the work has been done on simple systems comprised of inert matrices such as silica or cellulose. Recently, this process as been expanded to environmental samples as well [11,12]. -
Precision Cleaning Applications
CHAPTER 3 PRECISION CLEANING APPLICATIONS 3.1. BACKGROUND Precision cleaning applications are characterised by the extremely fine level of cleanliness required to keep delicate instruments and surfaces operating effectively. Although precision cleaning is needed in a wide variety of industries, several key factors define the applications where precision cleaning is required. These include those applications in which (1) critical cleanliness standards of particulate and/or organic contaminants need to be satisfied, (2) components have sensitive compatibilities, (3) components I $ have physical characteristics such as geometry and porosity which make dewatering crucial in the cleaning process, and (4) components being cleaned are costly. A variety of particulate and nonparticulate contaminants are removed in precision cleaning operations. Particulate contamination includes scrap material created during cutting, drilling, grinding, and buffing of precision parts (e.g., silicon wafers and aluminum storage disk substrates). Nonparticulate contamination includes waxes, finger print oils, and other contaminants. As the term suggests precision cleaning involves cleaning components to extremely strict standards of cleanliness. A good indication of the cleaning ability required for precision cleaning processes is provided in Figure 111-1, which shows the clearance on a computer disk drive relative to the size of various contaminants. The factor that made CFC-113 the precision cleaning solvent of choice is its remarkable chemical stability (manifested directly in its compatibility to structural materials), its low toxicity, and zero flammability. This has * 1991 UNEP SOLVENTS. COATINGS, AND ADHESIVES REPORT * -1 31- Figure III-I SIZE COMPARISON OF COMPUTER DISK DRIVE HEAD CLEARANCE WITH VARIOUS CONTAMINANTS ' !! allowed closed, superclean, white-room assembly areas to be operated safely and effectively. -
Cleaning with Supercritical Carbon Dioxide
Cleaning with Supercritical Carbon Dioxide Ken Laintz and Dale Spall Los Alamos NATIONAL LABORATORY Chemical Science and Technology Organic Analytical Chemistry CST-12, MS E537 Los Alamos, New Mexico 87545 (505) 665-3545, FAX (505) 667-6561 Outline Supercritical Fluids Cleaning Operations using Supercritial Fluid Solvents Experimental Cleaning Results Other Cleaning Applications Significant Properties of Supercritical Fluids 0 High diffusivity results in high mass transfer 0 Low viscosity and surface tension results in small pore penetration 0 High density results in solvent properties similar to liquids 0 Density is a selective function of temperature and pressure Solute Extraction and Removal Kinetics Extraction Time Operational Economics of Cleaning Prospects Direct Labor Indirect Labor Factory Costs Labor Expenses Benefits Factory Overhead Depreciation Cycle Time Costs Maintenance New Technology Changeover Costs Facility Space Costs Consumables Consumables Disposal Costs Liability Costs Utilities Energy and Utilities Aqueous Supercritical CO2 Taxes and Fees Administration Semi-aqueous Finance Capital Costs Finance Charges Quality Cost of Quality JAAST Joint Association for the Advancement of Supercritical Fluid Technology Mission: To develop and disseminate SCF cleaning applications in support of environmentally conscious manufacturing to meet the needs of the government and industry Members Hughes Aerospace Applied Separations DOE U. Mass. Lowell Allied Signal Autoclave Engineers EPA U. South Carolina Ciba Vision CF Technologies SNL -
Development and Design of a High Pressure Carbon Dioxide System for the Separation of Hazardous Contaminants from Non-Hazardous Debris*
DEVELOPMENT AND DESIGN OF A HIGH PRESSURE CARBON DIOXIDE SYSTEM FOR THE SEPARATION OF HAZARDOUS CONTAMINANTS FROM NON-HAZARDOUS DEBRIS* Carol L. J. Adkins and Edward M. Russick <~~ 'f\ «//) - cj^'- - / ^ 61 Sandia National Laboratories, Albuquerque, NM -^ " H. Mike Smith and Ron B. Olson AlliedSignal Inc., Kansas City Division, Kansas City, MO ABSTRACT Under the Department of Energy (DOE)AJnited States Air Force (USAF) Memorandum of Understanding, a system is being designed that will use high pressure carbon dioxide for the separation of oils, greases, and solvents from non-hazardous solid waste. The contaminants are dissolved into the high pressure carbon dioxide and precipitated out upon depressurization. The carbon dioxide solvent can then be recycled for continued use. Excellent extraction capability for common manufacturing oils, greases, and solvents has been measured. It has been observed that extraction performance follows the dilution model if a constant flow system is used. The solvents tested are extremely soluble and have been extracted to 100% under both liquid and mild supercritical carbon dioxide conditions. These data are being used to design a 200 liter extraction system. KEY WORDS: Supercritical, Carbon dioxide, Cleaning 1. INTRODUCTION Large quantities of solid wastes such as rags, kimwipes, swabs, coveralls, gloves, etc., contaminated with oils, greases and hazardous solvents are generated by industry and the government. At present, these materials must be treated as hazardous waste, and the cost of disposal of such large volumes of hazardous materials is high. If the hazardous components (oils, greases and solvents) could be segregated from the much larger bulk of non-hazardous material, then these solid materials could potentially be handled as sanitary waste at significant cost savings. -
The Role of Supercritical CO2 in the Drying of Porous Silicon
Rev. Energ. Ren.: ICPWE (2003) 99-102 The Role of Supercritical CO2 in the Drying of Porous Silicon M. Bouchaour, N. Diaf, A. Ould-Abbas, M. Benosman, L. Merad and N-E. Chabane-Sari Laboratoire de Matériaux & Energies Renouvelables (LMER), Faculté des Sciences, Université Abou Bekr Belkaïd, B. P 119, Tlemcen,13000, Algérie. E-mail : [email protected] Abstract – The study of light emission from porous silicon has attracted great interest since the first observation of its photoluminescence at room temperature [1]. Recently, particular interest is devoted to supercritical fluid CO2 [2] applications on the drying of this semiconductor. This fluid is inotoxic, non- flammable, unreactive under most conditions, leaves no liquid waste. It has a potential to ameliorate environmental safety and health impact and it enables innovative processing technologies and material protection [3]. This talk reviews the mechanism of supercritical drying of porous silicon and the role of this fluid in this process. Résumé – L'étude de l'émission de la lumière du silicium poreux a attiré un grand intérêt depuis la première observation de la photoluminescence à la température ambiante [1]. Récemment, l'intérêt particulier est consacré aux applications du fluide supercritique CO2 [2] sur le séchage de ce semi-conducteur. Ce fluide est non toxique, inflammable. Il offre des possibilités intéressantes d'améliorer la sûreté environnementale et est utilisé dans des nouvelles technologies afin d’assurer la protection matérielle [3]. Ce papier concerne le mécanisme du séchage supercritique du silicium poreux et le rôle du fluide supercritique CO2 dans ce processus. Key-Words: Porous silicon – Supercritical drying – Supercritical fluid CO2. -
Liquid-Liquid Transition in Supercooled Aqueous Solution Involving a Low-Temperature Phase Similar to Low-Density Amorphous Water
Liquid-liquid transition in supercooled aqueous solution involving a low-temperature phase similar to low-density amorphous water * * # # Sander Woutersen , Michiel Hilbers , Zuofeng Zhao and C. Austen Angell * Van 't Hoff Institute for Molecular Sciences, University of Amsterdam, Science Park 904,1098 XH Amsterdam, The Netherlands # School of Molecular Sciences, Arizona State University, Tempe, AZ, 85287-1604, USA The striking anomalies in physical properties of supercooled water that were discovered in the 1960-70s, remain incompletely understood and so provide both a source of controversy amongst theoreticians1-5, and a stimulus to experimentalists and simulators to find new ways of penetrating the "crystallization curtain" that effectively shields the problem from solution6,7. Recently a new door on the problem was opened by showing that, in ideal solutions, made using ionic liquid solutes, water anomalies are not destroyed as earlier found for common salt and most molecular solutes, but instead are enhanced to the point of precipitating an apparently first order liquid-liquid transition (LLT)8. The evidence was a spike in apparent heat capacity during cooling that could be fully reversed during reheating before any sign of ice crystallization appeared. Here, we use decoupled-oscillator infrared spectroscopy to define the structural character of this phenomenon using similar down and upscan rates as in the calorimetric study. Thin-film samples also permit slow scans (1 Kmin-1) in which the transition has a width of less than 1 K, and is fully reversible. The OH spectrum changes discontinuously at the phase- transition temperature, indicating a discrete change in hydrogen-bond structure. -
Application of Supercritical Fluids Review Yoshiaki Fukushima
1 Application of Supercritical Fluids Review Yoshiaki Fukushima Abstract Many advantages of supercritical fluids come Supercritical water is expected to be useful in from their interesting or unusual properties which waste treatment. Although they show high liquid solvents and gas carriers do not possess. solubility solutes and molecular catalyses, solvent Such properties and possible applications of molecules under supercritical conditions gently supercritical fluids are reviewed. As these fluids solvate solute molecules and have little influence never condense at above their critical on the activities of the solutes and catalysts. This temperatures, supercritical drying is useful to property would be attributed to the local density prepare dry-gel. The solubility and other fluctuations around each molecule due to high important parameters as a solvent can be adjusted molecular mobility. The fluctuations in the continuously. Supercritical fluids show supercritical fluids would produce heterogeneity advantages as solvents for extraction, coating or that would provide novel chemical reactions with chemical reactions thanks to these properties. molecular catalyses, heterogenous solid catalyses, Supercritical water shows a high organic matter enzymes or solid adsorbents. solubility and a strong hydrolyzing ability. Supercritical fluid, Supercritical water, Solubility, Solvation, Waste treatment, Keywords Coating, Organic reaction applications development reached the initial peak 1. Introduction during the period from the second half of the 1960s There has been rising concern in recent years over to the 1970s followed by the secondary peak about supercritical fluids for organic waste treatment and 15 years later. The initial peak was for the other applications. The discovery of the presence of separation and extraction technique as represented 1) critical point dates back to 1822. -
Using Supercritical Fluid Technology As a Green Alternative During the Preparation of Drug Delivery Systems
pharmaceutics Review Using Supercritical Fluid Technology as a Green Alternative During the Preparation of Drug Delivery Systems Paroma Chakravarty 1, Amin Famili 2, Karthik Nagapudi 1 and Mohammad A. Al-Sayah 2,* 1 Small Molecule Pharmaceutics, Genentech, Inc. So. San Francisco, CA 94080, USA; [email protected] (P.C.); [email protected] (K.N.) 2 Small Molecule Analytical Chemistry, Genentech, Inc. So. San Francisco, CA 94080, USA; [email protected] * Correspondence: [email protected]; Tel.: +650-467-3810 Received: 3 October 2019; Accepted: 18 November 2019; Published: 25 November 2019 Abstract: Micro- and nano-carrier formulations have been developed as drug delivery systems for active pharmaceutical ingredients (APIs) that suffer from poor physico-chemical, pharmacokinetic, and pharmacodynamic properties. Encapsulating the APIs in such systems can help improve their stability by protecting them from harsh conditions such as light, oxygen, temperature, pH, enzymes, and others. Consequently, the API’s dissolution rate and bioavailability are tremendously improved. Conventional techniques used in the production of these drug carrier formulations have several drawbacks, including thermal and chemical stability of the APIs, excessive use of organic solvents, high residual solvent levels, difficult particle size control and distributions, drug loading-related challenges, and time and energy consumption. This review illustrates how supercritical fluid (SCF) technologies can be superior in controlling the morphology of API particles and in the production of drug carriers due to SCF’s non-toxic, inert, economical, and environmentally friendly properties. The SCF’s advantages, benefits, and various preparation methods are discussed. Drug carrier formulations discussed in this review include microparticles, nanoparticles, polymeric membranes, aerogels, microporous foams, solid lipid nanoparticles, and liposomes. -
A Review of Supercritical Fluid Extraction
NAT'L INST. Of, 3'«™ 1 lY, 1?f, Reference NBS PubJi- AlllDb 33TA55 cations /' \ al/l * \ *"»e A U O* * NBS TECHNICAL NOTE 1070 U.S. DEPARTMENT OF COMMERCE / National Bureau of Standards 100 LI5753 No, 1070 1933 NATIONAL BUREAU OF STANDARDS The National Bureau of Standards' was established by an act of Congress on March 3, 1901. The Bureau's overall goal is to strengthen and advance the Nation's science and technology and facilitate their effective application for public benefit. To this end, the Bureau conducts research and provides: (1) a basis for the Nation's physical measurement system, (2) scientific and technological services for industry and government, (3) a technical basis for equity in trade, and (4) technical services to promote public safety. The Bureau's technical work is per- formed by the National Measurement Laboratory, the National Engineering Laboratory, and the Institute for Computer Sciences and Technology. THE NATIONAL MEASUREMENT LABORATORY provides the national system ot physical and chemical and materials measurement; coordinates the system with measurement systems of other nations and furnishes essential services leading to accurate and uniform physical and chemical measurement throughout the Nation's scientific community, industry, and commerce; conducts materials research leading to improved methods of measurement, standards, and data on the properties of materials needed by industry, commerce, educational institutions, and Government; provides advisory and research services to other Government agencies; develops, -
OP03 Contribution of Computational Fluid Dynamics And
OP03 Contribution of Computational Fluid Dynamics and Thermodynamics to the development of supercritical carbon dioxide extraction processes Renan RAVETTI DURAN, Mouna LAZRAG, Romain PRIVAT, Cécile LEMAITRE, Danielle BARTH* Laboratoire Réactions et Génie des Procédés, UMR CNRS 7274, Université de Lorraine 1 rue Grandville-BP20451-54001 NANCY-France * [email protected] ABSTRACT In supercritical CO2 extraction process , there are two essential steps: the extraction step in the extractor where the SC-CO2 allows the solvent or extract removal from product structure and the separation step which consists of the separation of CO2-solvents or CO2-extract in a cascade of cyclone separators downstream the extractor. Cyclone separators are separation devices that use the centrifugal and gravity forces to remove liquid phase from flue gases. Two supercritical extraction processes are studied here: organogels supercritical drying for aerogels production and supercritical extraction of polar compounds from natural products. Concerning the first process, the organogel is prepared by an aminoacid-type organogelator with aromatic solvents such as tetralin or toluene. The experimental results showed a good solvent recovery rate in the case of tetralin, exceeding 90% but an unsatisfactory separation for toluene with a yield below 65%. In order to understand the experimental results a thermodynamic study and a hydrodynamic study (CFD) of the mixture separation in the cyclones are carried out. Supercritical extraction of polar compounds from natural products using a CO2 + aqueous ethanol mixture as solvent requires a reliable knowledge of vapor-liquid equilibria of the carbon dioxide + ethanol + water system in order to size and optimize the extraction process. -
Supercritical Fluid Carbon Dioxide Cleaning of Plutonium Parts
I SUPERCRITICAL FLUID CARBON DIOXIDE BACKGROUND CLEANING OF PLUTONIUM PARTS A supercritical fluid is the comprcssed, dense gas phase Stephanie J. Hale above the critical temperature. Liquefaction of a gas can EG&G Rocky Flats, Inc occur upon compression below the critical temperature, but above the critical temperature the gas cannot liquefy regardleas of the applied pressure and a single gas phase is ABSTRACT maintained. The critical point for carbon dioxide is 31'C and 74 bar (1088 psi) which means that the supercritical Supercritical fluid carbon dioxide is under investigation in fluid can be aUnined under relatively mild conditions. this work for use as a cleaning solvent for the final cleaning of plutonium parts. These parts must be free of The phase diagram of CO, (Figure 1) shows the organic residue to avoid cormsion in the stockpile. Initial supcrcritical region above 74 bar and the 32" isotherm. It studies on stainless steel and full-scale mock-up parts can be seen that very liquid-like densities can be achieved indicate that the oils of interest are easily and adequately and still remain in the gas phase. cleaned from the metal surfaces with supercritical fluid carbon dioxide. Results from compatibility studies show that undesirable oxidation or other surface mctions are not occurring during cxposureof plutonium to the supercritical fluid. Cleaning studies indicate that the oils of interest are Temperalure ' removed from the plutonium surface under relatively mild conditions. These studies indicate that supercritical fluid carbon dioxide is a very promising cleaning medium for this application. INTRODUCTION Our aim in this work is to develop a cleaning process that van u-o clean plutonium parts.