Recovery and Purification of Ionic Liquids from Solutions: a Review
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United States Patent 19 11 Patent Number: 5,364,534 Anselme Et Al
US005364534A United States Patent 19 11 Patent Number: 5,364,534 Anselme et al. 45 Date of Patent: Nov. 15, 1994 54 PROCESS AND APPARATUS FOR 4,872,991 10/1989 Kartels et al. ...................... 210/651 TREATING WASTE LIQUIDS 5,093,072 8/1991 Hitotsuyanagi et al. ........... 210/650 5,154,830 10/1992 Paul et al. ........................... 210/639 75 Inventors: Christophe Anselme, Le Vesinet; Isabelle Baudin, Nanterre, both of FOREIGN PATENT DOCUMENTS France 2628337 9/1989 France . 73 Assignee: Lyonnaise Des Eaux - Dumez, 4018994 1/1992 Japan ................................ 210/195.2 Nanterre, France Primary Examiner-Frank Spear (21) Appl. No.: 129,387 Assistant Examiner-Ana Fortuna Attorney, Agent, or Firm-Pollock, Vande Sande & 22 Filed: Sep. 30, 1993 Priddy (30) Foreign Application Priority Data 57 ABSTRACT Oct. 2, 1992 FR France ................................ 92 1699 Process for purifying and filtering fluids, especially 51l Int. Cl............................................... BOD 61/00 water, containing suspended contaminants and using 52 U.S. Cl. .................................... 210/650; 210/660; gravity separation means as well as membrane separa 210/800; 210/805; 210/195.1; 210/195.2; tion means, in a finishing stage, comprising the step of 210/257.2 introducing a pulverulent reagent into the fluid stream 58) Field of Search ............... 210/650, 639, 800, 790, to be treated downstream of the gravity separation and 210/195.1, 195.2, 295, 805, 900, 257.2, 660 upstream of the membrane separation, wherein said 56) References Cited pulverulent reagent is recycled from the purge of the U.S. PATENT DOCUMENTS membrane separation means to the upstream of the gravity separation means. -
Refinery Wastewater Management Using Multiple Angle Oil-Water Separators
REFINERY WASTEWATER MANAGEMENT USING MULTIPLE ANGLE OIL-WATER SEPARATORS Kirby S. Mohr, P.E. Mohr Separations Research, Inc. 1278 FM 407 Suite 109 Lewisville, TX 75077 Phone: 918-299-9290 Cell: 918-269-8710 John N. Veenstra, Ph.D., P.E., Oklahoma State University Dee Ann Sanders, Ph.D., P.E. Oklahoma State University A paper presented at the International Petroleum Environment Conference in Albuquerque, New Mexico, 1998 ABSTRACT In this work, an overview of oil-water separation, as used in the petroleum refining industries, is presented along with case studies. Discussions include: impact of solids, legal aspects, and differing types of systems currently in use, along with their advantages and disadvantages. Performance information on separators is presented with an emphasis on new multiple angle coalescing plate technology for refinery wastewater management. Several studies are presented including a large (20,000 US GPM flow rate) system recently installed at a major US refinery. The separator was constructed by converting two existing API separators into four separators, and adding multiple angle coalescing plates to increase throughput and efficiency. A year of operating experience with this system indicates good performance and few problems. Other examples provide information on separators installed in the United States and other countries. Keywords: Oil-water separator, multiple angle, coalescence, refinery, wastewater management, petroleum, coalescing plate technology BACKGROUND AND INTRODUCTION Oil has been refined for various uses for at least 1000 years. An Arab handbook written by Al-Razi, in approximately 865 A.D., describes distillation of “naft” (naphtha) for use in lamps and thus the beginning of oil refining (Forbes). -
Mixing Oil-Based Microencapsulation of Garlic Essential Oil: Impact of Incorporating Three Commercial Vegetable Oils on the Stability of Emulsions
foods Article Mixing Oil-Based Microencapsulation of Garlic Essential Oil: Impact of Incorporating Three Commercial Vegetable Oils on the Stability of Emulsions Yunjiao Zhao 1, Rui Liu 1,* , Cuiping Qi 1, Wen Li 1, Mohamed Rifky 1, Min Zhang 2,*, Ping Xiao 3, Tao Wu 1 and Wenjie Sui 1 1 State Key Laboratory of Food Nutrition and Safety, Tianjin University of Science & Technology, Tianjin 300457, China; [email protected] (Y.Z.); [email protected] (C.Q.); [email protected] (W.L.); [email protected] (M.R.); [email protected] (T.W.); [email protected] (W.S.) 2 College of Food Science and Bioengineering, Tianjin Agricultural University, Tianjin 300384, China 3 Tianjin Chunfa Bio-Technology Group Co., Ltd., Tianjin 300300, China; [email protected] * Correspondence: [email protected] (R.L.); [email protected] (M.Z.) Abstract: The active components in garlic essential oil are easily degradable, which limits its ap- plication in the food industry. Vegetable oils (VOs) were used to improve the stability of garlic essential oil (GEO) emulsion. The volatile compounds of GEO and its mixtures with vegetable oils (VOs), including corn oil (CO), soybean oil (SO), and olive oil (OO) indicated that GEO-VO mixtures had a higher percentage of Diallyl disulfide and Diallyl trisulfide than pure GEO. Adding an appropriate amount of VOs promoted the GEO emulsion (whey protein concentrate and inulin as Citation: Zhao, Y.; Liu, R.; Qi, C.; Li, the wall materials) stability in order of CO > SO > OO. Evaluation of the encapsulation efficiency, W.; Rifky, M.; Zhang, M.; Xiao, P.; Wu, controlled release, and antimicrobial activity of GEO-VO microcapsules showed that the GEO was T.; Sui, W. -
Distillation Accessscience from McgrawHill Education
6/19/2017 Distillation AccessScience from McGrawHill Education (http://www.accessscience.com/) Distillation Article by: King, C. Judson University of California, Berkeley, California. Last updated: 2014 DOI: https://doi.org/10.1036/10978542.201100 (https://doi.org/10.1036/10978542.201100) Content Hide Simple distillations Fractional distillation Vaporliquid equilibria Distillation pressure Molecular distillation Extractive and azeotropic distillation Enhancing energy efficiency Computational methods Stage efficiency Links to Primary Literature Additional Readings A method for separating homogeneous mixtures based upon equilibration of liquid and vapor phases. Substances that differ in volatility appear in different proportions in vapor and liquid phases at equilibrium with one another. Thus, vaporizing part of a volatile liquid produces vapor and liquid products that differ in composition. This outcome constitutes a separation among the components in the original liquid. Through appropriate configurations of repeated vaporliquid contactings, the degree of separation among components differing in volatility can be increased manyfold. See also: Phase equilibrium (/content/phaseequilibrium/505500) Distillation is by far the most common method of separation in the petroleum, natural gas, and petrochemical industries. Its many applications in other industries include air fractionation, solvent recovery and recycling, separation of light isotopes such as hydrogen and deuterium, and production of alcoholic beverages, flavors, fatty acids, and food oils. Simple distillations The two most elementary forms of distillation are a continuous equilibrium distillation and a simple batch distillation (Fig. 1). http://www.accessscience.com/content/distillation/201100 1/10 6/19/2017 Distillation AccessScience from McGrawHill Education Fig. 1 Simple distillations. (a) Continuous equilibrium distillation. -
Chem Tech Pro 2F/20, Jaljyoti Appartment, New Sama Road, Chhani Jakat Naka, Vadodara-390002 Website: Email: [email protected]
Suppliers of all types of Equipments, Instruments and Chemicals Hub for all types Equipments, Instruments and Chemicals for various industries Registered Marketing Office: Chem Tech Pro 2F/20, Jaljyoti Appartment, New Sama Road, Chhani Jakat Naka, Vadodara-390002 Website: www.chemtechpro.in Email: [email protected] 1 About Chem Tech Pro Chem Tech Pro is global leading suppliers of various scientific equipments, chemical equipments, educational equipments, pilot plants for chemicals and pharmaceuticals products, analytical instruments, automation systems, labo- ratory chemicals, industrial chemicals and varieties of technical services pro- vider. Chem Tech Pro’s Products and Services 1. Absorption Columns 2. Adsorption Columns 3. Agitators 4. Analytical Equipments 5. Boilers and Steam Generators 6. Catalysts 7. Centrifuges 8. Chemicals 9. Cooling Towers 10. Crystallizers 11. Decanters 12. Distillation Columns 13. Dryers 14. Educational Equipments for Engineering Colleges 15. Environmental Equipments 16. Evaporators 17. Extraction Units 18. Fans, Blowers and Compressors 19. Fermenters and Bioreactors 20. Furnaces 21. Glass Equipments 22. Heat Exchangers 23. Humidifiers 24. Ion Exchange Equipments 25. Liquid Handling Equipments 26. Material Handling Equipments 27. Mechanical Seals and Stuffing Boxes 28. Membrane and Filtration Equipments 29. Mixing and Blending Units 30. Packing for columns 31. Personal Protective Equipments 32. Pilot Plants Specialists 33. Polymers 34. Pressure Vessels 35. Process Controllers and Instruments 36. Pumps 37. Reactors 38. Re-boilers 39. Safety and Fire fighting Equipments 40. Sewage Treatment Plants 41. Sight Glass and Flow Indicators 42. Solar Equipments 43. Sonicators and Homogenizers 44. Storage Tanks 45. Surface Treatment Equipments 46. Technical Services for various industries 47. Thickeners and Clarifiers 48. -
A Marine Waste Biorefinery
A Marine Waste Biorefinery A thesis submitted for the degree of Doctor of Philosophy (PhD) at Newcastle University by Ahmed Said Hamed Al Hatrooshi November 2019 Abstract Biodiesel is a renewable alternative to ‘petro-diesel’. There is already an established, conventional production technology based on refined vegetable oils. However, this is always more expensive than producing petroleum-based diesel, mainly due to the feedstock cost. Use of a cheap, non- edible feedstock, such as waste shark liver oil (WSLO), would reduce the biodiesel production cost and make the process economically viable. WSLO is obtained by exposing sharks’ livers to the sun until they melt and collecting the oil produced. Sharks’ livers comprise 25-30% of their body weight. Historically, the discarded WSLO was used for waterproofing wooden boats. However, this application is no longer required, as modern boats are made of fibreglass. The excess WSLO derived from these discarded sharks’ livers has great potential for being further processed into valuable products, including biodiesel, squalene and omega-3 polyunsaturated fatty acids (PUFA), such as eicosapentaenoic (EPA) and docosahexaenoic (DHA). The glyceride components of the WSLO can be converted into biodiesel using existing biodiesel processing technologies, while the squalene, EPA and DHA may be extracted and sold as value-added products through biorefinery processes. This study investigated the production of fatty acid methyl ester (FAME) from WSLO using both acid (sulfuric acid, H2SO4) and base (sodium hydroxide, NaOH) catalysts. Due to the high levels of free fatty acids (FFA) in WSLO, homogeneous alkali-catalysed transesterification was less effective than the acid-catalysed process, resulting in a maximum WSLO to FAME conversion of only 40% after 15 min at a 60°C temperature, a 1.5 wt.% of NaOH catalyst and a 6:1 molar ratio of methanol to WSLO. -
Lithium Isotope Separation a Review of Possible Techniques
Canadian Fusion Fuels Technology Project Lithium Isotope Separation A Review of Possible Techniques Authors E.A. Symons Atomic Energy of Canada Limited CFFTP GENERAL CFFTP Report Number s Cross R< Report Number February 1985 CFFTP-G-85036 f AECL-8 The Canadian Fusion Fuels Technology Project represents part of Canada's overall effort in fusion development. The focus for CFFTP is tritium and tritium technology. The project is funded by the governments of Canada and Ontario, and by Ontario Hydro. The Project is managed by Ontario Hydro. CFFTP will sponsor research, development and studies to extend existing experience and capability gained in handling tritium as part of the CANDU fission program. It is planned that this work will be in full collaboration and serve the needs of international fusion programs. LITHIUM ISOTOPE SEPARATION: A REVIEW OF POSSIBLE TECHNIQUES Report No. CFFTP-G-85036 Cross Ref. Report No. AECL-8708 February, 1985 by E.A. Symons CFFTP GENERAL •C - Copyright Ontario Hydro, Canada - (1985) Enquiries about Copyright and reproduction should be addressed to: Program Manager, CFFTP 2700 Lakeshore Road West Mississauga, Ontario L5J 1K3 LITHIUM ISOTOPE SEPARATION: A REVIEW OF POSSIBLE TECHNIQUES Report No. OFFTP-G-85036 Cross-Ref Report No. AECL-87O8 February, 1985 by E.A. Symons (x. Prepared by: 0 E.A. Symons Physical Chemistry Branch Chemistry and Materials Division Atomic Energy of Canada Limited Reviewed by: D.P. Dautovich Manager - Technology Development Canadian Fusion Fuels Technology Project Approved by: T.S. Drolet Project Manager Canadian Fusion Fuels Technology Project ii ACKNOWLEDGEMENT This report has been prepared under Element 4 (Lithium Compound Chemistry) of the Fusion Breeder Blanket Program, which is jointly funded by AECL and CFFTP. -
Enrichment of Natural Products Using an Integrated Solvent-Free Process: Molecular Distillation
BK1064-ch62_R2_250706 SYMPOSIUM SERIES NO. 152 # 2006 IChemE ENRICHMENT OF NATURAL PRODUCTS USING AN INTEGRATED SOLVENT-FREE PROCESS: MOLECULAR DISTILLATION Fregolente, L.V.; Moraes, E.B.; Martins, P.F.; Batistella, C.B.; Wolf Maciel, M.R.; Afonso, A.P.; Reis, M.H.M. Chemical Engineering School/Separation Process Development Laboratory (LDPS) State University of Campinas – CP 6066 – CEP 13081-970 – Campinas – SP – Brazil E-mail: [email protected] Molecular distillation is a potential process for separation, purification and/or concentration of natural products, usually constituted by complex and thermally sen- sitive molecules, such as vitamins. Furthermore, this process has advantages over other techniques that use solvents as the separating agent, avoiding problems of toxi- city. This process is characterized by short exposure of the distilled liquid to high temperatures, by high vacuum (around 1024 mmHg) in the distillation space and by a small distance between the evaporator and the condenser (around 2 cm). The pro- ductivity of the process is high, considering the concentration of high added value compounds. In this work, the molecular distillation process was applied to enrich borage oil in gamma-linolenic acid (GLA) and also to recover tocopherols from deo- dorizer distillate of soybean oil (DDSO), since these are components of interest for food and pharmaceutical industries. KEYWORDS: gamma-linolenic acid, vitamin E, molecular distillation, deodorizer distillate of soybean oil, borrage oil INTRODUCTION Molecular distillation shows potential in the separation, purification and/or concentration of natural products, usually constituted by complex and thermally sensitive molecules, such as vitamins and polyunsaturated fatty acids, because it can minimize losses by thermal decomposition. -
Separation of Tocopherol from Crude Palm Oil Biodiesel
ISSN 2090-424X J. Basic. Appl. Sci. Res., 1(9)1169-1172, 2011 Journal of Basic and Applied © 2011, TextRoad Publication Scientific Research www.textroad.com Separation of Tocopherol from Crude Palm Oil Biodiesel Hendrix Yulis Setyawan1*, Erliza hambali 2, Ani Suryani2, Dwi Setyaningsih 2 1 Department of Industrial Agricultural Technology, Faculty of Agricultural, University of Brawijaya Veteran Street Malang City East Java Indonesia Phone: +62341580106 Fax: +62341568917 2 Departments of Industrial Agricultural Technology, Faculty of Agricultural, Bogor Agricultural University Baranangsiang Campus IPB, Jl Raya Bogor Pajajaran 16,153 ABSTRACT A molecular distillation procedure was developed to extract tocopherols from crude palm oil based biodiesel. Change of CPO to biodiesel can be made by esterification and transesterification reaction. Use of esterification and trans-esterification reaction were facilitated the process of molecular distillation because of the heavy molecules such as glycerol have been separated first. The conditions of molecular distillation to recover tocopherols were set-up of with a flow rate of 1.3 liter/jam-1, 7 liters / hour, distillation temperature 175 ˚ C - 220 ˚ C and 200 rpm rotational speed wipers - 400 rpm. It was found that the yield of tocopherols were the separated between 22.9 mg - 605 mg from 1.302 mg of overall tocopherol content in crude palm oil based biodiesel. The overall recovery of tocopherols was around 35% of the original content in crude palm oil based biodiesel. In the residue, there were no different value in acid number, FFA content, density, kinematic viscosity and iodine value of crude palm oil based biodiesel after molecular distillation process. -
Design and Feasibility Analysis of Commercial Silver-Based Solvent Extraction of Omega-3 Pufa by Kirubanandan Shanmugam, Andrew Neima & Adam A
Global Journal of Researches in Engineering: J General Engineering Volume 15 Issue 5 Version 1.0 Year 2015 Type: Double Blind Peer Reviewed International Research Journal Publisher: Global Journals Inc. (USA) Online ISSN: 2249-4596 Print ISSN:0975-5861 Design and Feasibility Analysis of Commercial Silver-Based Solvent Extraction of Omega-3 Pufa By Kirubanandan Shanmugam, Andrew Neima & Adam A. Donaldson Dalhousie University, Canada Abstract- Afish oil processing facility was designed and evaluated for the annual extraction of 2.5 ktonnes of Omega-3 polyunsaturated fatty acids from 18/12EE fish oils by liquid-liquid solvent extraction through the use of a silver-based solvent. Using experimentally derived extraction efficiencies obtained with commercial 18/12EE fish oil, a plug-flow reactor configuration is proposed to significantly reduce silver solvent inventory requirements relative to conventional batch processes, corresponding to an initial capital reduction of ~$40 million at this scale. Evaluation of the proposed facilityresulted in capital costs of $4.9 million, annual operating costs of $7.7million, and a yearly gross revenue of $21.0 million. Considering the expensive solvent used, the profitability of the proposed process is highly dependent on the amount of solvent required to fill the vessels, and on the recovery efficiency following de-complexation of the Omega-3 and silver ions. Depending on market conditions, a number of recovery methods are discussed and evaluated, with specific emphasis placed on chemical, thermal or electrolytic methods. Keywords: EPA/DHA, fish oils, solvent extraction, silver, omega-3, processdesign, solvent inventory. GJRE-J Classification : FOR Code: 291899 DesignandFeasibilityAnalysisofCommercialSilverBasedSolventExtractionofOmega3Pufa Strictly as per the compliance and regulations of : © 2015. -
Method and Apparatus for Cryopreparation, Dry Stabilization and Rehydration of Biological Suspensions
Europaisches Patentamt European Patent Office © Publication number: 0 475 409 A2 Office europeen des brevets EUROPEAN PATENT APPLICATION © Application number: 91115480.5 int. CI 5= A01N 1/02, F26B 5/06 @ Date of filing: 12.09.91 ® Priority: 12.09.90 US 581584 8654 Plum Lake Drive, Houston, 03.06.91 US 709504 Texas 77095(US) Inventor: Nichols, Ken B. @ Date of publication of application: 16106 La Cabana, Houston, 18.03.92 Bulletin 92/12 Texas 77062(US) Inventor: Piunno, Carmen © Designated Contracting States: 9,Glory Bower, The Woodlands, AT BE CH DE DK ES FR GB GR IT LI LU NL SE Texas 77381 (US) Inventor: Ross, David © Applicant: LIFECELL CORPORATION 19735 San Gabriel, Houston, 3606-A Research Forest Drive Texas 77081 (US) The Woodlands, Texas 77381 (US) @ Inventor: Livesey, Stephen © Representative: Dost, Wolfgang, 104 Napoleon St Eltham, Victoria Dr.rer.nat.,Dipl.-Chem. et al austria 3000(US) Patent- & Rechtsanwalte Bardehle . Inventor: Del Campo, Anthony A. Pagenberg . Dost . Altenburg . Frohwitter . 11810 Oakcroft, Houston, Geissler & Partner Galileiplatz 1 Postfach 86 Texas 77381 (US) 06 20 Inventor: Nag, Abhijit W-8000 Munchen 86(DE) © Method and apparatus for cryopreparation, dry stabilization and rehydration of biological suspensions. © This invention relates to methods, apparatus and solutions for cryopreserving microscopic biological materials for biologically extended periods of time. The method comprises treating a suspension of biological material, in a appropriate buffer, with a cryoprotectant or combination of cryoprotectants which raises the glass transition temperature range of the sample. One or more dry protectants may be added to the cryosolution. The cryosolution is then nebulized and rapidly cooled with novel apparatus, dried by molecular distillation, stored and then rehydrated in a buffer prior to its use. -
Chapter 15. Gravity Separation
Chapter 15. Gravity Separation IS. INTRODUCTION Separation by density difference is a process that is as old as recorded history. Separation of gold by density difference dates back to at least 3,000 BC as depicted in writings from ancient Egypt. The principle employed in gravity separation goes back further in time to the formation and weathering of the rocks and the releasing of the minerals they contain and the transport of the mineral grains by heavy rains. It is the driving force for the formation of the alluvial deposits of precious metals and gemstones that have been worked since beyond recorded history as they still are today. Archaeological excavations have discovered mineral concentration activities such as the lead-silver concentrating plant in Attica, Greece, dating from 300-400 BC. So gravity separation has a long history as a mineral concentration process. Not all mineral combinations are amenable to this type of concentration technique. To determine the suitability of gravity separation processes to a particular ore type, a concentration criterion is commonly used. A concentration criterion (CC) can be defined as [1]: „ . „. SG of heavy mineral-SG of fluid ,<-,.. Concentration Criterion = (15.1) SG of light mineral - SG of fluid where SG = specific gravity (or density), and the fluid is typically water or air. Some concentration criterion ratios for minerals that are treated by gravity separation are given in Table 15.1. Table 15.1 Concentration criterion for some common minerals separated by gravity separation from a gangue of density 2650 kg/m3 Mineral Fluid CC Gold water 10.3 Gold air 6.8 Cassiterite water 3.5 Coal water 3.4 Hematite water 2.5 A guideline for separability by gravity based on this concentration criterion is given in Table 15.2.