Health and Environmental Effects Profile for Isobutanol
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Safety Data Sheet
SAFETY DATA SHEET Revision Date 13-Dec-2020 Revision Number 6 SECTION 1: IDENTIFICATION OF THE SUBSTANCE/MIXTURE AND OF THE COMPANY/UNDERTAKING 1.1. Product identifier Product Description: Neopentyl alcohol Cat No. : 128250000; 128250100; 128250500 Synonyms 2,2-Dimethyl-1-propanol CAS-No 75-84-3 EC-No. 200-907-3 Molecular Formula C5 H12 O 1.2. Relevant identified uses of the substance or mixture and uses advised against Recommended Use Laboratory chemicals. Uses advised against No Information available 1.3. Details of the supplier of the safety data sheet Company UK entity/business name Fisher Scientific UK Bishop Meadow Road, Loughborough, Leicestershire LE11 5RG, United Kingdom EU entity/business name Acros Organics BVBA Janssen Pharmaceuticalaan 3a 2440 Geel, Belgium E-mail address [email protected] 1.4. Emergency telephone number For information US call: 001-800-ACROS-01 / Europe call: +32 14 57 52 11 Emergency Number US:001-201-796-7100 / Europe: +32 14 57 52 99 CHEMTREC Tel. No.US:001-800-424-9300 / Europe:001-703-527-3887 SECTION 2: HAZARDS IDENTIFICATION 2.1. Classification of the substance or mixture CLP Classification - Regulation (EC) No 1272/2008 Physical hazards Flammable solids Category 2 (H228) Health hazards ______________________________________________________________________________________________ ACR12825 Page 1 / 10 SAFETY DATA SHEET Neopentyl alcohol Revision Date 13-Dec-2020 ______________________________________________________________________________________________ Acute Inhalation Toxicity - Dusts and Mists (H332) Category 4 Specific target organ toxicity - (single exposure) (H335) Category 3 (H336) Environmental hazards Based on available data, the classification criteria are not met Full text of Hazard Statements: see section 16 2.2. -
Isobutanol in Marine Gasoline
Isobutanol in Marine Gasoline Glenn Johnston July 11, 2017 Bioeconomy 2017 Washington D.C. 1B: Drivers for Emergence of Biofuels for Maritime Industry © 2012 Gevo, Inc. | 1 Gevo’s Current Business System Gevo Production Facilities Core Near Term Markets Isobutanol Production – Side-by-Side with Ethanol Drop-in Markets - Isobutanol Luverne, MN Isobutanol Specialty Chemicals & Solvents Specialty Gasoline Blendstock (Marine/Off-Road) 15 MGPY EtOH 1.5 MGPY IBA* Isobutanol Hydrocarbon Biorefinery Drop-in Markets - Hydrocarbons South Hydrocarbons Hampton Jet Fuel Resources Silsbee, TX Isooctane (gasoline) © 2016 Gevo, Inc. | 2 Isobutanol Properties Gasoline blending value Gasoline Ethanol Isobutanol RON 95 109 105 MON 85 90 91 Anti-knock Index 90 100 98 RVP (psi) 7-15 19 5.2 Density 20C [kg/m3] 720-775 794 801 Boiling Point (C) 32.2 21.1 26.6 % Heating Value of Gasoline 100 66 84 Oxygen (%w/w) <2.7% 34.7 21.6 isobutanol has low RVP, enabling refiners to blend incremental volumes of butanes and pentanes Marine Research Overview Marine Engine Tested – BRP Envinrude and SeaDoo, Mercury, Volvo-Penta, Yamaha, Tohatsu, Indmar, OMC-Johnson, Honda. Marine Biobutanol over 5 years of research -Alternative Fuel Butanol: Preliminary Investigation on Performance and Emissions of a Marine Two-Stroke Direct Fuel Injection Engine -Impact of Blending Gasoline with lsobutanol Compared to Ethanol on Efficiency, Performance and Emissions of a Recreational Marine 4-Stroke Engine -Gaseous and Particulate Emissions Using Isobutanol-Extended Fuel in Recreational Marine -
Next Generation Biofuels
Photo-Synthetic Biology for Fuels James C. Liao Chemical and Biomolecular Engineering University of California, Los Angeles The Current Biofuel Cycle CO2 CO2 Ethanol Biodiesel The Direct Solar Fuel Cycle CO2 CO2 Higher Alcohols Biofuels Long chain Ethanol alcohols/alkanes Energy content Low High Hygroscopicity High Low Vehicle Yes No retrofitting? Vapor pressure High Low Production High Zero/Low yield Higher alcohols Native producers? yes Iso-propanol no n-propanol yes n-butanol no Iso-butanol no 2-methyl-1-butanol no 3-methyl-1-butanol Pathways for alcohol synthesis CoA-dependent pathway Pyruvate PDH NADH Acetyl-CoA Acetaldehyde NADH NADH ADH Acetoacetyl-CoA Ethanol 3-Hydroxybutyryl-CoA Crotonyl-CoA Butyryl-CoA Butyraldehyde n-Butanol Alternative Pathways to Make Alcohols CoA-dependent pathway Pyruvate Non-CoA pathway PDH NADH PDC Acetyl-CoA Acetaldehyde NADH NADH ADH ? Acetoacetyl-CoA Ethanol 3-Hydroxybutyryl-CoA Crotonyl-CoA Butyryl-CoA Butyraldehyde n-Butanol Atsumi et al. Nature 2008 Generalization of keto acid decarboxylase chemistry Longer chain keto acids A simple keto acid Pyruvate 2-keto acid PDC KDC Acetylaldehyde R-aldehyde ADH ADH Ethanol R-OH Ehrlich, F. Ber. Dtsch. Chem. Ges.1907 Opening the active site Zymomonas mobilis PDC Lactococcus lactis KdcA E.coli Long Chain 2-keto acids KDC 2-keto acids) R-aldehyde ADH 2008 2-phenylethanol (from Nature 3-M-1-butanol et al. 2-M-1-butanol p henylpyruvate Atsumi Production of Higher Alcohols1-butanol in 2-keto-4-methyl-pentanoate 2-keto-3-methyl-valerate isobutanol 2-ketovalerate 1-propanol 2-ketoisovalerate Production (mM) Production 2-ketobutyrate ํC 40hr 30 Further generalization of alcohol‐ producing chemistry Atsumi et al. -
Ester Synthesis Lab (Student Handout)
Name: ________________________ Lab Partner: ____________________ Date: __________________________ Class Period: ____________________ Ester Synthesis Lab (Student Handout) Lab Report Components: The following must be included in your lab book in order to receive full credit. 1. Purpose 2. Hypothesis 3. Procedure 4. Observation/Data Table 5. Results 6. Mechanism (In class) 7. Conclusion Introduction The compounds you will be making are also naturally occurring compounds; the chemical structure of these compounds is already known from other investigations. Esters are organic molecules of the general form: where R1 and R2 are any carbon chain. Esters are unique in that they often have strong, pleasant odors. As such, they are often used in fragrances, and many artificial flavorings are in fact esters. Esters are produced by the reaction between alcohols and carboxylic acids. For example, reacting ethanol with acetic acid to give ethyl acetate is shown below. + → + In the case of ethyl acetate, R1 is a CH3 group and R2 is a CH3CH2 group. Naming esters systematically requires naming the functional groups on both sides of the bridging oxygen. In the example above, the right side of the ester as shown is a CH3CH2 1 group, or ethyl group. The left side is CH3C=O, or acetate. The name of the ester is therefore ethyl acetate. Deriving the names of the side from the carboxylic acid merely requires replacing the suffix –ic with –ate. Materials • Alcohol • Carboxylic Acid o 1 o A o 2 o B o 3 o C o 4 Observation Parameters: • Record the combination of carboxylic acid and alcohol • Observe each reactant • Observe each product Procedure 1. -
Safety Data Sheet
SAFETY DATA SHEET 1. Identification Product identifier 1-OCTEN-3-OL, (AMYL VINYL CARBINOL) FCC Other means of identification BRI Product Code 160 CAS number 3391-86-4 FEMA number 2805 Synonyms 1-Octen-3-ol * Matsutake alcohol * Mushroom Alcohol * Pentyl vinyl carbinol * Vinyl pentyl carbinol Recommended use flavors and fragrances For Manufacturing Use Only Recommended restrictions Not for use in Tobacco or Nicotine delivery device applications and/or products. Manufacturer/Importer/Supplier/Distributor information Manufacturer Company name Bedoukian Research Address 6 Commerce Drive Danbury, CT 06810 United States Telephone 1-203-830-4000 Website www.bedoukian.com E-mail [email protected] Contact person Joseph Bania Emergency phone number Chemtrec (North America) 1-800-424-9300 Chemtrec (International) 1-703-527-3887 2. Hazard(s) identification Physical hazards Flammable liquids Category 4 Health hazards Acute toxicity, oral Category 3 Acute toxicity, inhalation Category 4 Skin corrosion/irritation Category 2 Serious eye damage/eye irritation Category 2A Environmental hazards Hazardous to the aquatic environment, acute Category 2 hazard Hazardous to the aquatic environment, Category 3 long-term hazard OSHA defined hazards Not classified. Label elements Signal word Danger Hazard statement Combustible liquid. Toxic if swallowed. Causes skin irritation. Causes serious eye irritation. Toxic to aquatic life. Harmful to aquatic life with long lasting effects. Harmful if inhaled. Precautionary statement Prevention Keep away from flames and hot surfaces-No smoking. Wash thoroughly after handling. Do not eat, drink or smoke when using this product. Avoid release to the environment. Wear protective gloves/eye protection/face protection. Material name: 1-OCTEN-3-OL, (AMYL VINYL CARBINOL) FCC SDS US 160 Version #: 05 Revision date: 23-October-2018 Issue date: 25-May-2015 1 / 9 Response If swallowed: Immediately call a poison center/doctor. -
Method MD-99 Polar Volatile Organic Compounds in Pulp Industry Wastewaters by Microdistillation and GC-FID
NCASI METHOD MD-99 POLAR VOLATILE ORGANIC COMPOUNDS IN PULP INDUSTRY WASTEWATERS BY MICRODISTILLATION AND GC-FID NCASI West Coast Regional Center Organic Analytical Program July 1999 Acknowledgments This method is authored by Alex Gholson, Senior Research Scientist, and Dean Hoy, Research Associate, with assistance from Diana Cook, Senior Research Scientist, all of NCASI West Coast Regional Center. Mark Bruce of Wadsworth Alert Labs (now Quanterra) developed the microdistillation technique and also provided valuable input during development of this method. For more information about this method, contact: Alex Gholson, Ph.D. John Pinkerton, Ph.D. Senior Research Scientist Vice President, Air Quality NCASI West Coast Regional Center NCASI P.O. Box 458 P.O. Box 13318 Corvallis, OR 97339 Research Triangle Park, NC 27709 (541) 752-8801 (919) 558-1992 [email protected] [email protected] For information about NCASI publications, contact: Publications Coordinator NCASI PO Box 13318 Research Triangle Park, NC 27709 (919) 558-1999 [email protected] National Council for Air and Stream Improvement, Inc. (NCASI). 2000. Methods Manual - Polar volatile organic compounds in pulp industry wastewaters by microdistillation and GC-FID. Research Triangle Park, NC: National Council for Air and Stream Improvement, Inc. 2000 by the National Council for Air and Stream Improvement, Inc. Disclaimer: The mention of trade names or commercial products does not constitute endorsement or recommendation for use. The microdistillation step has been included in the Third Update of SW-846 as Method 5031. This method is included in the NCASI Methods Manual as a PROPOSED method. The purpose of including proposed methods in the NCASI Methods Manual is to make it known that a method is under development and to solicit comment regarding the technical merit and applicability of the method. -
Toxicological Review of Tert-Butyl Alcohol (Tert-Butanol)
EPA/635/R-16/079a Public Comment Draft www.epa.gov/iris Toxicological Review of tert-Butyl Alcohol (tert-Butanol) (CAS No. 75-65-0) April 2016 NOTICE This document is a Public Comment Draft. This information is distributed solely for the purpose of pre-dissemination peer review under applicable information quality guidelines. It has not been formally disseminated by EPA. It does not represent and should not be construed to represent any Agency determination or policy. It is being circulated for review of its technical accuracy and science policy implications. National Center for Environmental Assessment Office of Research and Development U.S. Environmental Protection Agency Washington, DC Toxicological Review of tert-Butyl Alcohol DISCLAIMER This document is a preliminary draft for review purposes only. This information is distributed solely for the purpose of pre-dissemination peer review under applicable information quality guidelines. It has not been formally disseminated by EPA. It does not represent and should not be construed to represent any Agency determination or policy. Mention of trade names or commercial products does not constitute endorsement or recommendation for use. This document is a draft for review purposes only and does not constitute Agency policy. ii DRAFT—DO NOT CITE OR QUOTE Toxicological Review of tert-Butyl Alcohol CONTENTS AUTHORS | CONTRIBUTORS | REVIEWERS ................................................................................................. viii PREFACE ....................................................................................................................................................... -
Alcohol to Jet - Isobutanol
Alcohol to Jet - Isobutanol Glenn Johnston Vice President Regulatory Affairs Gevo Inc. Session 3 – Next in the Production Line: What to Expect for Future Development and Production of Aviation Alternative Fuels Biocatalyst Gevo integrated Isobutanol Alcohol (yeast) fermentation to Jet technology (ATJ) (GIFT®) Alcohol to Hydrocarbons • Sugar to Isobutanol fermentation facility owned by Gevo and producing renewable isobutanol. • Location – Luverne, MN • Creating the feedstock for our demonstration scale ATJ process in Silsbee, Texas • Proprietary processing based on standard unit operations in a typical petroleum refinery. • Gevo has been producing jet fuel since 2011 with over 5 years of process performance data on process capability and feedstock, including QA/QC process control charts to 6 SIGMA. • Process yields have been shown at 98% of theoretical. Process Flow Isobutanol Isobutylene C8-C16 olefins i-BuOH Isooctane Oligomerization Hydrogenation Dehydration Distillation separator 2 - phase Jet Water ASTM D7566 Annex 5 Standard Specification for Aviation Turbine Fuel Containing Synthesized Hydrocarbons A5. ALCOHOL-TO-JET SYNTHETIC PARAFFINIC KEROSENE (ATJ-SPK) ASTM D1655 Property Typical Jet A-1 Specification ATJ-SPK (Test Method) (CRC 647) (Jet A/Jet A-1) Freezing Point -40°C max Jet A - 50°C <-80°C (ASTM D2386) -47°C max Jet A-1 Flash Point 38°C min 48°C 48°C (ASTM D3828) Energy Density (Net Heat of Combustion) 42.8 MJ/kg min 42.9 MJ/kg 43.2 MJ/kg (ASTM D3338) Thermal Oxidation Stability (JFTOT) pass pass pass (ASTM D3241) Total Sulfur Content 0.3% max 0.05% <0.01% (ASTM D2622) • Extensive Quality Control Process of each lot which includes requirements from ASTM, Joint Inspection Group (JIG), DEFSTAN 91- 91 and others. -
Pdf 586.72 K
Regular Article ORGANIC CHEMISTRY RESEARCH Published by the Iranian Chemical Society www.orgchemres.org Org. Chem. Res., Vol. 3, No. 1, 73-85, March 2017. A Tandem Scalable Microwave-Assisted Williamson Alkyl Aryl Ether Synthesis under Mild Conditions M. Javaheriana,*, F. Kazemib, S.E. Ayatib, J. Davarpanahb and M. Ramdarb aDepartment of Chemistry, Faculty of Sciences, Shahid Chamran University of Ahvaz, Iran. Ahvaz, Golestan Blvd, P. O. Box: 6135743135 bDepartment of Chemistry, University for Advanced Studies in Basic Sciences, Zanjan, Iran. Gava Zang, Zanjan, 45195-1159, Iran (Received 10 July 2016, Accepted 7 June 2017) An efficient tandem synthesis of alkyl aryl ethers, including valuable building blocks of dialdehyde and dinitro groups under microwave irradiation and solvent free conditions on potassium carbonate as a mild solid base has been developed. A series of alkyl aryl ethers were obtained from alcohols in excellent yields by following the Williamson ether synthesis protocol under practical mild conditions. Scale up ability of this practical procedure is shown by the preparation of some of the valuable dialdehydes up to 50 mmole from alcohols. The method is simple, rapid, straight-forward and holds potential for further application in organic synthesis and industrial requirements. Keywords: Tandem, scalable, Williamson ether synthesis, Alkyl tosylate, Microwave irradiation, Bis-2-nitrophenoxy akyl ether, Bis-2- formylphenoxy alkyl ether INTRODUCTION solvents [17,18], narrow substrate scopes [19], or noncommercial sophisticated catalysts [20], with long Alkyl aryl ethers are important solvents and synthetic reaction times [21], and also harsh reaction conditions, building blocks for the production of fragrances, cosmetics, which limits the attractiveness of some of these methods, pharmaceuticals and dyestuffs with emphasis on derivatives especially for large-scale or industrial applications. -
A Feasibility Study of Cellulosic Isobutanol Production—Process Simulation and Economic Analysis
processes Article A Feasibility Study of Cellulosic Isobutanol Production—Process Simulation and Economic Analysis Avraam Roussos 1,*, Nikiforos Misailidis 1, Alexandros Koulouris 2, Francesco Zimbardi 3 and Demetri Petrides 4 1 Intelligen Europe, 57001 Thessaloniki, Greece; [email protected] 2 Alexander Technological Education Institute of Thessaloniki, 57400 Thessaloniki, Greece; [email protected] 3 Trisaia Research Centre, ENEA, 75026 Rotondella, Italy; [email protected] 4 Intelligen Inc., Scotch Plains, NJ 07076, USA; [email protected] * Correspondence: [email protected]; Tel.: +30-694-726-0939 Received: 21 June 2019; Accepted: 25 September 2019; Published: 27 September 2019 Abstract: Renewable liquid biofuels for transportation have recently attracted enormous global attention due to their potential to provide a sustainable alternative to fossil fuels. In recent years, the attention has shifted from first-generation bioethanol to the production of higher molecular weight alcohols, such as biobutanol, from cellulosic feedstocks. The economic feasibility of such processes depends on several parameters such as the cost of raw materials, the fermentation performance and the energy demand for the pretreatment of biomass and downstream processing. In this work, two conceptual process scenarios for isobutanol production, one with and one without integrated product removal from the fermentor by vacuum stripping, were developed and evaluated using SuperPro Designer®. In agreement with previous publications, it was concluded that the fermentation titer is a crucial parameter for the economic competitiveness of the process as it is closely related to the energy requirements for product purification. In the first scenario where the product titer was 22 g/L, the energy demand for downstream processing was 15.8 MJ/L isobutanol and the unit production cost of isobutanol was $2.24/L. -
Safety Data Sheet
SAFETY DATA SHEET Flammable Liquefied Gas Mixture: Ethanol / Isobutanol / Isopropanol (Isopropyl Alcohol) / Methanol / N-Butane / N-Butanol (N-Butyl Alcohol) / N-Propanol / Sec-Butyl Alcohol (2-Butanol) / Tert Butanol Section 1. Identification GHS product identifier : Flammable Liquefied Gas Mixture: Ethanol / Isobutanol / Isopropanol (Isopropyl Alcohol) / Methanol / N-Butane / N-Butanol (N-Butyl Alcohol) / N-Propanol / Sec-Butyl Alcohol (2-Butanol) / Tert Butanol Other means of : Not available. identification Product use : Synthetic/Analytical chemistry. SDS # : 011439 Supplier's details : Airgas USA, LLC and its affiliates 259 North Radnor-Chester Road Suite 100 Radnor, PA 19087-5283 1-610-687-5253 Emergency telephone : 1-866-734-3438 number (with hours of operation) Section 2. Hazards identification OSHA/HCS status : This material is considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200). Classification of the : FLAMMABLE GASES - Category 1 substance or mixture GASES UNDER PRESSURE - Liquefied gas GHS label elements Hazard pictograms : Signal word : Danger Hazard statements : Extremely flammable gas. Contains gas under pressure; may explode if heated. May cause frostbite. May form explosive mixtures in Air. May displace oxygen and cause rapid suffocation. Precautionary statements General : Read and follow all Safety Data Sheets (SDS’S) before use. Read label before use. Keep out of reach of children. If medical advice is needed, have product container or label at hand. Close valve after each use and when empty. Use equipment rated for cylinder pressure. Do not open valve until connected to equipment prepared for use. Use a back flow preventative device in the piping. Use only equipment of compatible materials of construction. -
Isobutanol and Drinking Water (PDF)
HEALTH RISK ASSESSMENT UNIT Isobutanol and Drinking Water Isobutanol is a contaminant that has been found in waters that could be used as drinking water sources in Minnesota. The Minnesota Department of Health (MDH) developed a health-based guidance value for isobutanol in drinking water and, based on this value and levels found in drinking water, does not expect isobutanol in drinking water will harm Minnesotans. Summary Isobutanol is used as a solvent and chemical manufacturing ingredient in several industries and may be used as a biofuel. The first commercial isobutanol biofuel site opened in Minnesota in 2012. Isobutanol has been found in stormwater runoff and groundwater in Minnesota. Isobutanol Isobutanol is used as a solvent in the flavor, fragrance, pharmaceutical, and pesticide industries and as a chemical manufacturing ingredient for products such as lacquer, paint strippers, paint primer, and craft paints. It is an approved food additive and is also naturally-occurring in some foods and many alcoholic beverages. Isobutanol may also be used as a biofuel because, like ethanol, it can be manufactured from corn and other plants. The first commercial bio-based isobutanol site in the United States opened in 2012 at a converted ethanol plant in southwestern Minnesota.1 A second plant was converted from ethanol to isobutanol production by 2015. Isobutanol in Minnesota Waters Isobutanol has been detected in stormwater runoff near an isobutanol production site in Minnesota at levels between 98 and 308 parts per billion (ppb). This runoff flows to a retaining pond which may be connected to local groundwater. Isobutanol has been detected in groundwater monitoring wells near landfills at levels between 74.5 and 105 ppb.2 MDH Guidance Value Based on available information, MDH developed a guidance value of 300 ppb for isobutanol in water.3 A person drinking water at or below the guidance value would have little or no risk of health effects.