Effect of Solvents and Extraction Methods on Recovery of Bioactive Compounds from Defatted Gac (Momordica Cochinchinensis Spreng.) Seeds

Total Page:16

File Type:pdf, Size:1020Kb

Effect of Solvents and Extraction Methods on Recovery of Bioactive Compounds from Defatted Gac (Momordica Cochinchinensis Spreng.) Seeds separations Article Effect of Solvents and Extraction Methods on Recovery of Bioactive Compounds from Defatted Gac (Momordica cochinchinensis Spreng.) Seeds Anh V. Le 1,2,* ID , Sophie E. Parks 1,3 ID , Minh H. Nguyen 1,4 and Paul D. Roach 1 1 School of Environmental and Life Sciences, University of Newcastle, Ourimbah, NSW 2258, Australia; [email protected] (S.E.P.); [email protected] (M.H.N.); [email protected] (P.D.R.) 2 Faculty of Bio-Food Technology and Environment, University of Technology (HUTECH), Ho Chi Minh City 700000, Vietnam 3 Central Coast Primary Industries Centre, NSW Department of Primary Industries, Ourimbah, NSW 2258, Australia 4 School of Science and Health, Western Sydney University, Penrith, NSW 2751, Australia * Correspondence: [email protected] Received: 3 July 2018; Accepted: 23 July 2018; Published: 30 July 2018 Abstract: Gac (Momordica cochinchinensis Spreng.) seeds contain bioactive compounds with medicinal properties. This study aimed to determine a suitable solvent and extraction technique for recovery of important compounds, namely, trypsin inhibitors, saponins, and phenolics. The antioxidant capacity and total solids of derived extracts were also measured. Water with conventional extraction method gave the highest value of trypsin inhibitor activity (118.45 ± 4.90 mg trypsin g−1) while water-saturated n-butanol and methanol extracts were characterized by their highest content of saponins (40.75 ± 0.31 and 38.80 ± 2.82 mg AE g−1, respectively). Aqueous extract with microwave assistance achieved the highest phenolics (3.18 ± 0.04 mg GAE g−1). As a measure of antioxidant capacity, the 2,20-azino-bis(3-ethylbenzothiazoline-6-sulfonic acid) diammonium salt (ABTS) assay gave highest value to the aqueous microwave extract (23.56 ± 0.82 µmol TE g−1) while the ferric reducing antioxidant power (FRAP) assay gave highest values to water-saturated n-butanol and 70% ethanol extracts (5.25 ± 0.04 and 4.71 ± 0.39 µmol TE g−1, respectively). The total solids value was highest using water with microwave assistance (141.5 g kg−1) while ultrasound treatment did not improve any extractions. Therefore, trypsin inhibitors are suitably recovered using water while water-saturated n-butanol or methanol is for saponins, both using a conventional method. Microwave extraction is suitable for phenolics recovery. These conditions are recommended for an efficient recovery of bioactive compounds from defatted Gac seeds. Keywords: Gac seeds; MAE; UAE; Momordica cochinchinensis; trypsin inhibitors; saponins; phenolics 1. Introduction Gac (Momordica cochinchinensis Spreng.) is a plant species of the family Cucurbitaceae, whose fruit is also known as red melon, baby jackfruit, spiny bitter gourd, sweet gourd and cochinchin gourd. It is native to the Southeast Asian region and is commonly grown as a crop in countries like Vietnam, Thailand, Laos, Myanmar, and Cambodia [1,2]. The most important part of the mature fruit is the red flesh surrounding the seeds, called the aril, which is used as a colourant in rice or as a material for further processing into functional food ingredients [3]. The seeds are not eaten; they are removed from the aril and are mostly considered waste [3]. However, in traditional medicine, Gac seeds are purported to have a wide array of therapeutic effects Separations 2018, 5, 39; doi:10.3390/separations5030039 www.mdpi.com/journal/separations Separations 2018, 5, 39 2 of 13 on a wide variety of conditions, such as fluxes, liver and spleen disorders, haemorrhoids, wounds, bruises, swelling, and pus [2,4]. Several constituents have been identified, which could be involved in the medicinal effects of Gac seeds. These include trypsin inhibitors, such as MCoTI-I, MCoTI-II, and MCoTI-III [5–7]; saponins, such as Momordica Saponin I (Gypsoside), Momordica Saponin II (Quillaic acid) [8,9]; and phenolic compounds such as gallic acid and p-hydroxybenzoic acids [10]. However, studies on how to efficiently extract these various components from Gac seeds are scarce and they are vital for facilitating future applications for these bioactives. For any given plant bioactive, extractive yield depends on the extraction solvent, the chemical nature of the targeted component, and the characteristics of the extraction procedure. When other factors are kept constant, the extraction solvent plays a key role in obtaining the target constituents in terms of desired quality and quantity [11,12]. The choice of the solvent is mainly done based on the chemical properties, that is, polarity or hydrophobicity, of the target compounds. Organic solvents with medium or high polarity have been most commonly used in laboratories dealing with natural products and there is evidence that some extracts from these solvents have better activity compared with aqueous extracts [11]. However, organic solvents present safety and environmental issues. Due to the hydrophylic nature of the trypsin inhibitors and phenolics, and the amphiphilic properties of saponins in Gac seeds, aqueous solvents and the alcohols are the safest and the most environmentally-friendly solvents for the extraction of these compounds [13,14]. The conventional aqueous solvent extraction technique, in which the solid material is suspended in water with no assistance for breaking the cell structure of the solid material, is often associated with a long heating time, which risks the degradation of bioactive compounds. This has led to the proposed use of advanced techniques such as microwave-assisted extraction (MAE) and ultrasonic-assisted extraction (UAE) that are efficient in terms of extraction time and water consumption. In MAE, microwave heating is able to disrupt the plant cell structure via an increase in the internal pressure of the cell, thereby releasing the bioactive compounds [15]. Similarly, ultrasonic cavitation during UAE produces shockwaves that are also capable of disrupting the plant cell structure and releasing the plant bioactives [16]. These two advanced extraction methods were reported to be more efficient than the conventional method for recovering carotenoids in Gac peel [17]. They have been widely used for the recovery of bioactive compounds from plant materials and are considered the dominant trends in “green chemistry” extractions [18]. In the present study, it was hypothesised that MAE and UAE would be better than the conventional aqueous extraction technique for the recovery of the important bioactive compounds from Gac seeds. Therefore, the extraction of trypsin inhibitors, saponins, and phenolic compounds, as well as the antioxidant activity of extracts from Gac seeds, using MAE and UAE was compared to conventional extraction with water. Furthermore, the efficiency of extraction for the MAE and UAE techniques was also compared to other alcohol solvents, namely methanol, 50% methanol, ethanol, 70% ethanol, and water-saturated n-butanol. To date, no study has focused on assisted systems of aqueous extraction for the recovery of bioactive compounds from Gac seeds. The findings will be useful in the selection of best extraction methods specifically for the recovery of trypsin inhibitors, saponins, and phenolic compounds. 2. Materials and Methods 2.1. Materials 2.1.1. Solvents, Reagents, and Chemicals Solvents, including ethanol, methanol, and n-butanol, and chemicals, including vanillin, sulphuric acid, and potassium persulfate were purchased from Merck (Darmstadt, Germany). Folin-ciocalteu’s phenol reagent, anhydrous sodium carbonate, sodium nitrite, ferric chloride, gallic acid, 2,4,6-Tris (2-pyridyl)-s-triazine; (±)-6-hydroxy-2,5,7,8-tetramethylchromane-2carboxylic acid (Trolox), aecsin, 2,20-azino-bis(3ethylbenzothiazoline-6-sulfonic acid) diammonium salt (ABTS), trypsin (type I) from Separations 2018, 5, 39 3 of 13 bovine pancreas, benzyl-DL-arginine-para-nitroanilide (BAPNA), tris, and dimethylsulfoxide (DMSO) were from Sigma-Aldrich Co. (Castle Hill, NSW, Australia). Sodium acetate trihydrate was purchased from Government Stores Department (Kingswood, NSW, Australia). Acetic acid was obtained from BDH Laboratory Supplies (Poole, UK). Sodium hydroxide was from Ajax FineChem (Taren Point, NSW, Australia) and hydrochloride acid was obtained from Lab-scan Ltd. (Bangkok, Thailand). 2.1.2. Gac Seeds Gac seeds were collected from 450 kg of fresh Gac fruit from accession VS7 as classified by Wimalasiri et al. [1]. These fruits were bought at Gac fruit fields in Dong Nai province, Ho Chi Minh city, Vietnam (Latitude: 10.757410; Longitude: 106.673439). After their separation from the fresh fruit, the seeds were vacuum dried at 40 ◦C for 24 h to reduce moisture and increase the crispness of the shell, which would facilitate shell removal. The dried seeds were de-coated to get the kernels, which were then packaged in vacuum-sealed aluminium bags and stored at −18 ◦C until used. Preparation of Defatted Gac Seed Powder Gac seed kernels were ground in an electric grinder (100 g ST-02A Mulry Disintegrator), to pass through a sieve of 1.4 mm. The powder was then freeze-dried (Dynavac FD3 Freeze Dryer (Sydney, NSW, Australia)) for 48 h at −45 ◦C under vacuum at a pressure loading of 10−2 mbar (1 Pa), to reduce the moisture content to 12.1 ± 0.2 g kg–1. The powder was then defatted using hexane (1:5 w/v, 30 min, ×3) on a magnetic stirrer at room temperature. The resulting slurry was suction filtered and the residue (defatted powder) was air-dried for 12 h and stored in a desiccator at room temperature until used. The moisture content of the meal was recorded prior to weighing for extraction, using a MOC63u moisture analyzer (Shimazdu, Kyoto, Japan). 2.2. Methods 2.2.1. Extraction Methods Initially, for the conventional extraction (CE) method, there were six extraction solvents: water (DIW), pure methanol (Methanol), 50% methanol (Methanol50%), pure ethanol (Ethanol), 70% ethanol (Ethanol70%), and water-saturated n-butanol (Butanol), examined for the extraction of bioactive compounds from Gac seeds. For the two assisting methods of UAE and MAE, only water was chosen to investigate because in the CE method it was much better than the other solvents in terms of the extraction yield of trypsin inhibitors and phenolic compounds.
Recommended publications
  • Extraction Methods and Their Influence on Yield When Extracting Thermo-Vacuum-Modified Chestnut Wood
    Article Extraction Methods and Their Influence on Yield When Extracting Thermo-Vacuum-Modified Chestnut Wood Maurizio D’Auria 1 , Marisabel Mecca 1, Maria Roberta Bruno 2 and Luigi Todaro 2,* 1 Department of Science, University of Basilicata, Viale dell’Ateneo Lucano 10, 85100 Potenza, Italy; [email protected] (M.D.); [email protected] (M.M.) 2 School of Agricultural Forestry, Food, and Environmental Science, University of Basilicata, Viale dell’Ateneo Lucano 10, 85100 Potenza, Italy; [email protected] * Correspondence: [email protected]; Tel.: +39-3478782534 Abstract: Improvements in the yield and solubility of chestnut wood extractives, by using different extraction methods and molybdenum catalysts as support, have rarely been reported in literature. Many studies focus on the different parts of trees, except for the chemical characteristics of the remaining extractives achieved from thermally modified (THM) chestnut (Castanea sativa Mill) wood. This research seeks to better understand the effects of extraction techniques and catalysts on the yield and solubility of extractives. GC-MS analysis of the chloroform soluble and insoluble fractions was also used. Accelerated Solvent Extraction (ASE) 110 ◦C, Soxhlet, and autoclave extraction techniques were used to obtain extractives from untreated and thermally modified (THM) chestnut ◦ wood (170 C for 3 h). Ethanol/H2O, ethanol/toluene, and water were the solvents used for each technique. A polyoxometalate compound (H3PMo12O40) and MoO3 supported on silica were used as catalysts. The THM induced a change in the wood’s surface color (DE = 21.5) and an increase in mass loss (5.9%), while the equilibrium moisture content (EMC) was reduced by 17.4% compared to the control wood.
    [Show full text]
  • Enhanced Butanol Production by Free and Immobilized Clostridium Sp
    Enhanced Butanol Production by Free and Immobilized Clostridium sp. Cells Using Butyric Acid as Co-Substrate Laili Gholizadeh This thesis comprises 30 ECTS credits and is a compulsory part in the Master of Science with a Major in Chemical Engineering – Applied Biotechnology 120 ECTS credits No. 10/2009 Title: Enhanced Butanol Production by Free and Immobilized Clostridium sp. Cells using Butyric Acid as Co-Substrate. Author: Laili Gholizadeh Baroghi (e-mail: [email protected]) Master Thesis Subject Category: Biotechnology (Bioprocess Engineering – Biofuels) University College of Borås School of Engineering SE-501 90 BORÅS Telephone: (+46) 033 435 4640 Examiner: Prof. Mohammad Taherzadeh Supervisor and Thesis Advisor: Prof. Shang–Tian Yang Supervisor Address: OSU–Ohio State University 125 Koffolt Laboratories 140 West 19th Ave. Columbus, OH 43210–1185, USA Client: Ohio State University (OSU), Chemical & Biomolecular Engineering Department Prof. Shang–Tian Yang Columbus, Ohio; USA. Date: 08–12–2009 Keywords: Bio-butanol y Acetone–Butanol–Ethanol (ABE) y ABE- fermentation y Butyric acid y Clostridium y C. acetobutylicum ATCC 824 y C. beijerinckii ATCC 55025 y C. beijerinckii BA 101 y C. beijerinckii NCIMB 8052 y Fibrous-bed Bioreactor (FBB) y Batch y Suspended cell culture y Immobilized cell system. DEDICATION I would like to dedicate this M.Sc. Thesis to my beloved Family for all their love and encouragement and for always been supportive of my choices. “I am among those who think that science has great beauty. A scientist in his laboratory is not only a technician: he is also a child placed before natural phenomena, which impress him like a fairy tale.” − Marie Curie ABSTRACT Butanol production by four different Clostridium sp.
    [Show full text]
  • Transcription 12.01.12
    Lecture 2B • 01/12/12 We covered three different reactions for converting alcohols into leaving groups. One was to turn an alcohol into an alkyl chloride, that was using thionyl chloride. Second reaction was using tosyl chloride; the primary difference between those two reactions is one of stereochemistry. An inversion of stereochemistry does occur if you use thionyl chloride, because it does affect the carbon-oxygen bond, but because forming a tosylate does not touch the carbon-oxygen bond, only the oxygen- hydrogen bond, there’s no change in stereochemistry there. We then saw phosphorus tribromide that reacts very similarly to the thionyl chloride; you get an alkyl bromide instead, but it also has inversion of configuration. The last reaction is not a new mechanism, it is just an Sn2 reaction, it’s called the Finkelstein reaction. Really this works, in a sense, off of Le Châtelier’s principle. In solution, in theory, sodium iodide can displace bromide, but sodium bromide can displace iodide, so you can have an Sn2 reaction that goes back and forth and back and forth and back and forth. Except, sodium iodide is somewhat soluble in acetone, while sodium chloride and sodium bromide are not. So, in fact, one of the things that we get out of this as a by-product is sodium bromide, which, again, is not soluble in acetone and therefore precipitates out and is no longer part of the reaction mixture, so there’s no reverse reaction possible. Because of this solubility trick, it allows this reaction to be pulled forward, which means you can get the alkyl iodide.
    [Show full text]
  • Aldehydes and Ketones
    Organic Lecture Series Aldehydes And Ketones Chap 16 111 Organic Lecture Series IUPAC names • the parent alkane is the longest chain that contains the carbonyl group • for ketones, change the suffix -e to -one • number the chain to give C=O the smaller number • the IUPAC retains the common names acetone, acetophenone, and benzophenone O O O O Propanone Acetophenone Benzophenone 1-Phenyl-1-pentanone (Acetone) Commit to memory 222 Organic Lecture Series Common Names – for an aldehyde , the common name is derived from the common name of the corresponding carboxylic acid O O O O HCH HCOH CH3 CH CH3 COH Formaldehyde Formic acid Acetaldehyde Acetic acid – for a ketone , name the two alkyl or aryl groups bonded to the carbonyl carbon and add the word ketone O O O Ethyl isopropyl ketone Diethyl ketone Dicyclohexyl ketone 333 Organic Lecture Series Drawing Mechanisms • Use double-barbed arrows to indicate the flow of pairs of e - • Draw the arrow from higher e - density to lower e - density i.e. from the nucleophile to the electrophile • Removing e - density from an atom will create a formal + charge • Adding e - density to an atom will create a formal - charge • Proton transfer is fast (kinetics) and usually reversible 444 Organic Lecture Series Reaction Themes One of the most common reaction themes of a carbonyl group is addition of a nucleophile to form a tetrahedral carbonyl addition compound (intermediate). - R O Nu - + C O Nu C R R R Tetrahedral carbonyl addition compound 555 Reaction Themes Organic Lecture Series A second common theme is
    [Show full text]
  • N-BUTYL ALCOHOL
    Right to Know Hazardous Substance Fact Sheet Common Name: n-BUTYL ALCOHOL Synonyms: Propyl Carbinol; n-Butanol CAS Number: 71-36-3 Chemical Name: 1-Butanol RTK Substance Number: 1330 Date: November 1998 Revision: January 2008 DOT Number: UN 1120 Description and Use EMERGENCY RESPONDERS >>>> SEE BACK PAGE n-Butyl Alcohol is a colorless liquid with a strong, sweet Hazard Summary alcohol odor. It is used as a solvent for fats, waxes, shellacs, Hazard Rating NJDOH NFPA resins, gums, and varnish, in making hydraulic fluids, and in HEALTH - 2 medications for animals. FLAMMABILITY - 3 REACTIVITY - 0 f ODOR THRESHOLD = 1 to 15 ppm FLAMMABLE f Odor thresholds vary greatly. Do not rely on odor alone to POISONOUS GASES ARE PRODUCED IN FIRE determine potentially hazardous exposures. CONTAINERS MAY EXPLODE IN FIRE Hazard Rating Key: 0=minimal; 1=slight; 2=moderate; 3=serious; Reasons for Citation 4=severe f n-Butyl Alcohol is on the Right to Know Hazardous f n-Butyl Alcohol can affect you when inhaled and by Substance List because it is cited by OSHA, ACGIH, DOT, passing through the skin. NIOSH, DEP, IRIS, NFPA and EPA. f Contact can irritate and burn the skin. f This chemical is on the Special Health Hazard Substance f n-Butyl Alcohol can irritate and burn the eyes with possible List. eye damage. f Inhaling n-Butyl Alcohol can irritate the nose, throat and lungs. f Exposure to n-Butyl Alcohol can cause headache, dizziness, nausea and vomiting. SEE GLOSSARY ON PAGE 5. f n-Butyl Alcohol can damage the liver, kidneys, hearing, and sense of balance.
    [Show full text]
  • Method 3520C: Continuous Liquid-Liquid Extraction, Part of Test
    METHOD 3520C CONTINUOUS LIQUID-LIQUID EXTRACTION 1.0 SCOPE AND APPLICATION 1.1 This method describes a procedure for isolating organic compounds from aqueous samples. The method also describes concentration techniques suitable for preparing the extract for the appropriate determinative steps described in Sec. 4.3 of Chapter Four. 1.2 This method is applicable to the isolation and concentration of water-insoluble and slightly soluble organics in preparation for a variety of chromatographic procedures. 1.3 Method 3520 is designed for extraction solvents with greater density than the sample. Continuous extraction devices are available for extraction solvents that are less dense than the sample. The analyst must demonstrate the effectiveness of any such automatic extraction device before employing it in sample extraction. 1.4 This method is restricted to use by or under the supervision of trained analysts. Each analyst must demonstrate the ability to generate acceptable results with this method. 2.0 SUMMARY OF METHOD 2.1 A measured volume of sample, usually 1 liter, is placed into a continuous liquid-liquid extractor, adjusted, if necessary, to a specific pH (see Table 1), and extracted with organic solvent for 18 - 24 hours. 2.2 The extract is dried, concentrated (if necessary), and, as necessary, exchanged into a solvent compatible with the cleanup or determinative method being employed (see Table 1 for appropriate exchange solvents). 3.0 INTERFERENCES 3.1 Refer to Method 3500. 3.2 The decomposition of some analytes has been demonstrated under basic extraction conditions required to separate analytes. Organochlorine pesticides may dechlorinate, phthalate esters may exchange, and phenols may react to form tannates.
    [Show full text]
  • 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,
    [Show full text]
  • Alcoholsalcohols
    AlcoholsAlcohols Chapter 10 1 Structure of Alcohols • The functional group of an alcohol is H an -OH group bonded to an sp3 O 108.9° hybridized carbon. C H – Bond angles about the hydroxyl oxygen H H atom are approximately 109.5°. • Oxygen is sp3 hybridized. –Two sp3 hybrid orbitals form sigma bonds to a carbon and a hydrogen. – The remaining two sp3 hybrid orbitals each contain an unshared pair of electrons. 2 Nomenclature of Alcohols • IUPAC names – The parent chain is the longest chain that contains the OH group. – Number the parent chain to give the OH group the lowest possible number. – Change the suffix -etoe -ol.ol • Common names – Name the alkyl group bonded to oxygen followed by the word alcohol.alcohol 3 Nomenclature of Alcohols OH o o 1o OH 1 2 OH 1-Propanol 2-Propan ol 1-Bu tanol (Pro py l alco ho l) (Isoprop yl alcoh ol) (Bu tyl alcoh ol) OH 2o OH 1o OH 3o 2-Butanol 2-M eth yl-1-p ropan ol 2-M eth yl-2-p ropan ol (sec-Butyl alcohol) (Isobutyl alcohol) (tert -Butyl alcohol) 4 Nomenclature of Alcohols • Compounds containing more than one OH group are named diols, triols, etc. CH2 CH2 CH3 CHCH2 CH2 CHCH2 OH OH HO OH HO HO OH 1,2-Ethanediol 1,2-Propanediol 1,2,3-Propanetriol (Ethylene glycol) (Propylene glycol) (Glycerol, Glycerine) 5 Physical Properties • Alcohols are polar compounds. – They interact with themselves and with other polar compounds by dipole-dipole interactions. • Dipole-dipole interaction: The attraction between the positive end of one dipole and the negative end of another.
    [Show full text]
  • 2.1.2 Extractive Crystallization
    EUROPEAN ROADMAP OF PROCESS INTENSIFICATION - TECHNOLOGY REPORT - TECHNOLOGY: EXTRACTIVE CRYSTALLIZATION TECHNOLOGY CODE: 2.1.2 AUTHOR: Mark Roelands, TNO Science & Industry, Delft, Netherlands Table of contents 1. Technology 1.1 Description of technology / working principle 1.2 Types and “versions” 1.3 Potency for Process Intensification: possible benefits 1.4 Stage of development 2. Applications 2.1 Existing technology (currently used) 2.2 Known commercial applications 2.3 Known demonstration projects 2.4 Potential applications discussed in literature 3. What are the development and application issues? 3.1 Technology development issues 3.2 Challenges in developing processes based on the technology 4. Where can information be found? 4.1 Key publications 4.2 Relevant patents and patent holders 4.3 Institutes/companies working on the technology 5. Stakeholders 5.1 Suppliers/developers 5.2 End-users 6. Expert’s brief final judgment on the technology 1 1. Technology 1.1 Description of technology / working principle (Feel free to modify/extend the short technology description below) Extractive crystallization is a hybrid process in which crystallization and extraction are combined. There are several process configurations possible. Either the solute or the solvent can be extracted from a solution. In case the solute is extracted, the solute accumulates in the extractant until this phase becomes supersaturated and crystallization starts. In one configuration a reactive extractant is applied. Subsequently the crystals are separated from the mother liquor. In this case the crystal are the desired product. In a second configuration absorption of a compound from a gas stream into a reactive extractant takes place, followed by crystallization of one of the compounds.
    [Show full text]
  • Strategies to Introduce N-Butanol in Gasoline Blends
    sustainability Article Strategies to Introduce n-Butanol in Gasoline Blends Magín Lapuerta *, Rosario Ballesteros and Javier Barba Escuela Técnica Superior de Ingenieros Industriales, University of Castilla-La Mancha, Av. Camilo José Cela s/n, 13071 Ciudad Real, Spain; [email protected] (R.B.); [email protected] (J.B.) * Correspondence: [email protected] Academic Editors: Gilles Lefebvre and Francisco J. Sáez-Martínez Received: 13 February 2017; Accepted: 7 April 2017; Published: 12 April 2017 Abstract: The use of oxygenated fuels in spark ignition engines (SIEs) has gained increasing attention in the last few years, especially when coming from renewable sources, due to the shortage of fossil fuels and global warming concern. Currently, the main substitute of gasoline is ethanol, which helps to reduce CO and HC emissions but presents a series of drawbacks such as a low heating value and a high hygroscopic tendency, which cause higher fuel consumption and corrosion problems, respectively. This paper shows the most relevant properties when replacing ethanol by renewable n-butanol, which presents a higher heating value and a lower hygroscopic tendency compared to the former. The test matrix carried out for this experimental study includes, on the one hand, ethanol substitution by n-butanol in commercial blends and, on the other hand, either ethanol or gasoline substitution by n-butanol in E85 blends (85% ethanol-15% gasoline by volume). The results show that the substitution of n-butanol by ethanol presents a series of benefits such as a higher heating value and a greater interchangeability with gasoline compared to ethanol, which makes n-butanol a promising fuel for SIEs in commercial blends.
    [Show full text]
  • Alcohols I 1400
    ALCOHOLS I 1400 Table 1 MW: Table 1 CAS: Table 2 RTECS: Table 2 METHOD: 1400, Issue 2 EVALUATION: PARTIAL Issue 1: 15 February 1984 Issue 2: 15 August 1994 OSHA : Table 2 PROPERTIES: Table 1 NIOSH: Table 2 ACGIH: Table 2 COMPOUNDS AND SYNONYMS: (1) ethanol: ethyl alcohol. (2) isopropyl alcohol: 2-propanol. (3) tert-butyl alcohol: 2-methyl-2-propanol. SAMPLING MEASUREMENT SAMPLER: SOLID SORBENT TUBE TECHNIQUE: GAS CHROMATOGRAPHY, FID (coconut shell charcoal, 100 mg/50 mg) ANALYTE: compounds above FLOW RATE: 0.01 to 0.2 L/min (£0.05 L/min for ethyl alcohol) DESORPTION: 1 mL 1% 2-butanol in CS 2 (1) (2) (3) INJECTION VOL-MIN: 0.1 L 0.3 L 1.0 L VOLUME: 5 µL -MAX: 1 L 3 L 10 L TEMPERATURE-INJECTION: 200 °C SHIPMENT: cooled -DETECTOR: 250-300 °C -COLUMN: 65-70 °C SAMPLE STABILITY: unknown, store in freezer CARRIER GAS: N2 or He, 30 mL/min BLANKS: 2 to 10 field blanks per set COLUMN: glass, 2 m x 4-mm ID, 0.2% Carbowax 1500 on 60/80 Carbopack C or equivalent ACCURACY CALIBRATION: solutions of analyte in eluent (internal standard optional) RANGE STUDIED: see EVALUATION OF METHOD RANGE AND BIAS: not significant [1] PRECISION: see EVALUATION OF METHOD OVERALL PRECISION (S ˆ ): see EVALUATION OF METHOD rT ESTIMATED LOD: 0.01 mg per sample [2] ACCURACY: ± 14% APPLICABILITY: The working ranges are 16 to 1000 ppm ethanol (30 to 1900 mg/m 3) for a 1-L air sample; 4 to 400 ppm isopropyl alcohol (10 to 1000 mg/m 3) for a 3-L air sample; and 1 to 100 ppm t-butyl alcohol (3 to 300 mg/m 3) for a 10-L air sample.
    [Show full text]
  • Liquid-Liquid Extraction Technology
    Liquid-Liquid Extraction Technology 0610 4501 Liquid-Liquid Extraction Technology at Sulzer Chemtech Sulzer Chemtech, a member of the Sulzer Corporation, with headquarters in Winterthur, Switzerland, is active in the field of process engineering, employing 3’000 persons worldwide. Sulzer Chemtech is represented in all important industrial countries setting standards in the field of mass transfer and static mixing with its advanced and economical solutions. Sulzer Chemtech is organized into four business units, one of which is the Process Technology group. This business unit was formed in early 2009 following the acquisition of Kühni, a Swiss company with more than 75 years experience in innovative separation processes. Today, Sulzer Chemtech Process Technology is headquartered in Allschwil (Basel), Switzerland. We provide a unique and wide portfolio of separation and application technologies, amongst which liquid-liquid extraction. Working Principle Fields of Application Liquid-liquid extraction is an important the liquids are transported countercur- Liquid-liquid extraction is a complex sepa- separation technology, with a wide range rently. The viscosity and interfacial tension ration process. An additional component of applications in the modern process in- are additional important parameters. has to be introduced as extractant, which dustry. The extraction process is based on makes other subsequent separation steps In nearly all liquid-liquid extraction pro- different solubilities of components in two necessary. Therefore, liquid-liquid extrac- cesses one of the liquids is dispersed into immiscible, or partially miscible, liquids. tion is mostly used when separation of the second liquid in the form of droplets. The components that need to be recov- components by distillation is either un- The key for a high process performance ered are extracted from the feed stream economical, or even impossible.
    [Show full text]