Extractives in Wood and Their Behaviour in Pulping
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Polar Semivolatile Organic Compounds in Biomass-Burning Emissions and Their Chemical Transformations During Aging in an Oxidation flow Reactor
Atmos. Chem. Phys., 20, 8227–8250, 2020 https://doi.org/10.5194/acp-20-8227-2020 © Author(s) 2020. This work is distributed under the Creative Commons Attribution 4.0 License. Polar semivolatile organic compounds in biomass-burning emissions and their chemical transformations during aging in an oxidation flow reactor Deep Sengupta, Vera Samburova, Chiranjivi Bhattarai, Adam C. Watts, Hans Moosmüller, and Andrey Y. Khlystov Desert Research Institute, 2215 Raggio Parkway, Reno, NV 89512, USA Correspondence: Vera Samburova ([email protected]) Received: 20 December 2019 – Discussion started: 23 January 2020 Revised: 7 May 2020 – Accepted: 18 May 2020 – Published: 16 July 2020 Abstract. Semivolatile organic compounds (SVOCs) emit- 350 g mol−1 decreased after OFR aging, while abundances ted from open biomass burning (BB) can contribute to chem- of low-MW compounds (e.g., hexanoic acid) increased. This ical and physical properties of atmospheric aerosols and indicated a significant extent of fragmentation reactions in also may cause adverse health effects. The polar fraction of the OFR. Methoxyphenols decreased after OFR aging, while SVOCs is a prominent part of BB organic aerosols, and thus a significant increase (3.7 to 8.6 times) in the abundance of it is important to characterize the chemical composition and dicarboxylic acids emission factors (EFs), especially maleic reactivity of this fraction. In this study, globally and region- acid (10 to 60 times), was observed. EFs for fresh and ratios ally important representative fuels (Alaskan peat, Moscow from fresh-to-aged BB samples reported in this study can be peat, Pskov peat, eucalyptus, Malaysian peat, and Malaysian used to perform source apportionment and predict processes agricultural peat) were burned under controlled conditions occurring during atmospheric transport. -
Resin Acids in Rosin (Colophony) Solder Flux Fume Laboratory Method Using Gas Chromatography
Health and Safety Executive Resin acids in rosin (colophony) solder flux fume Laboratory method using gas chromatography Scope 1 This method describes the measurement of time-weighted average concentrations of rosin (also known as colophony) based solder flux fume collected onto membrane filters with analysis of the resin acid components, after derivatisation, by gas chromatography (GC). Summary 2 A measured volume of air is drawn through a membrane filter mounted in a sampling head close to the breathing zone. The filter is solvent desorbed, the resin acids derivatised and then quantified using GC with a flame ionisation detector (FID). If confirmation of the resin acid components’ identities is required, samples may also be analysed by GC with a mass spectrometer (MS) detector. However, MS is not recommended for quantitative analysis as, unlike an FID, the MS detector gives different response factors for the various resin acids. The use of alternative methods not included in the MDHS series is acceptable provided they can demonstrate the accuracy and reliability appropriate to the application. Recommended sampling 3 For long-term exposures: Maximum sampling time: 8 hours; Sampling rate: 1–2 l-1min; Sampled volume: up to 960 litres. For short-term exposures: Sampling time: 15 mins; Sampling rate: 2 lmin-1; Sampled volume: 30 litres. Prerequisites 4 Users of this method will need to be familiar with the content of MDHS14.1 Safety 5 Users of this method should be familiar with normal laboratory practice and MDHS83/3 carry out a suitable risk assessment. It is the user’s responsibility to establish appropriate health and safety practices and to ensure compliance with regulatory requirements. -
Mountain Pine Beetle-Attacked Lodgepole Pine for Pulp and Papermaking
Operational extractives management from- mountain pine beetle-attacked lodgepole pine for pulp and papermaking Larry Allen and Vic Uloth Mountain Pine Beetle Working Paper 2007-15 Natural Resources Canada, Canadian Forest Service, Pacific Forestry Centre, 506 West Burnside Road, Victoria, BC V8Z 1M5 (250) 363-0600 • cfs.nrcan.gc.ca/regions/pfc Natural Resources Ressources naturelles Canada Canada Canadian Forest Service canadien Service des forêts Operational extractives management from mountain pine beetle-attacked lodgepole pine for pulp and papermaking Larry Allen and Vic Uloth Mountain Pine Beetle Initiative W orking Paper 2007œ15 Paprican 3800 W esbrook Mall Vancouver, B.C. V6S 2L9 Mountain Pine Beetle Initiative PO # 8.43 Natural Resources Canada Canadian Forest Service Pacific Forestry Centre 506 W est Burnside Road Victoria, British Columbia V8Z 1M5 Canada 2007 ≤ Her Majesty the Queen in Right of Canada 2007 Printed in Canada Library and Archives Canada Cataloguing in Publication Allen, Larry Operational extractives m anagem ent from m ountain pine beetle-attached lodgepole pine from pulp and paperm aking / Larry Allen and Vic Uloth. (Mountain Pine Beetle Initiative working paper 2007-15) "Mountain Pine Beetle Initiative, Canadian Forest Service". "MPBI Project # 8.43". "Paprican". Includes bibliographical references: p. Includes abstract in French. ISBN 978-0-662-46480-8 Cat. no.: Fo143-3/2007-15E 1. Pulping--British Colum bia--Quality control. 2. Pulping--Alberta--Quality control. 3. Paper m ills-- Econom ic aspects--British Colum bia. 4. Pulp m ills--Econom ic aspects--Alberta. 5. Lodgepole pine--Diseases and pests–Econom ic aspects. 6. Mountain pine beetle--Econom ic aspects. -
H4R Position on Rosin As One Substance For
H4R Position Statement on Rosin, Rosin Salts and Rosin Esters Registered as One Substance 7th February 2019 REACH registrations of Rosin, Rosin Salts and Rosin Esters H4R Position Statement on One Substance Registration Historically, various names, CAS, and EINECS numbers have existed for rosin. REACH1 mandates “One Substance – One Registration”. This obliged the Rosin registrants to carefully examine the composition of their substances of interest. They concluded that, although Rosin is historically listed under different names and EINECS and CASRNs (e.g. Rosin; Tall-oil rosin; Resin acids and rosin acids; etc.), it needed to be considered as one and the same substance. In addition, the registrants concluded that rosin is a chemical substance of Unknown or Variable Composition, Complex Reaction Products and Biological Materials (UVCB). In other words, rosin was listed on EINECS and CAS under different names, but the rosin registrants determined that differentiation was not justified and appropriate as these are the same UVCB substances. Therefore, Rosin with CAS 8050-09-7 was chosen. Appendix 1 to this document outlines the registrations that cover each of these substances. This decision and its rationale for one rosin registration is well documented in two papers: “Justification for grouping rosin and rosin derivatives into families” by Gary McCallister (Hercules), Bert Lenselink (Hexion), Jerrold Miller (Arizona Chemical), Bill Grady (Arizona Chemical) and Leon Rodenburg (Eastman Chemical), 24 August 20102 “Justification for considering Rosin as a Single Substance” by H4R Consortium, 22 February 20103 Based on these papers, it was concluded that, for rosin and the derived rosin salts, fortified rosin, fortified rosin salts, rosin esters and fortified rosin esters, the starting rosin is not relevant. -
8341 No Clean Flux Paste
8341 No Clean Flux Paste MG Chemicals UK Limited Version No: A-1.0 2 Issue Date:26/04/2018 Safety Data Sheet (Conforms to Regulation (EU) No 2015/830) Revision Date: 14/01/2021 L.REACH.GBR.EN SECTION 1 IDENTIFICATION OF THE SUBSTANCE / MIXTURE AND OF THE COMPANY / UNDERTAKING 1.1. Product Identifier Product name 8341 Synonyms SDS Code: 8341; 8341-10ML; 8341-10MLCA, 8341B-10ML | UFI: HGH0-205D-2003-EPAT Other means of identification No Clean Flux Paste 1.2. Relevant identified uses of the substance or mixture and uses advised against Relevant identified uses For use with leaded and unleaded solder during soldering process Uses advised against Not Applicable 1.3. Details of the supplier of the safety data sheet Registered company name MG Chemicals UK Limited MG Chemicals (Head office) Heame House, 23 Bilston Street, Sedgely Dudley DY3 1JA United Address 9347 - 193 Street Surrey V4N 4E7 British Columbia Canada Kingdom Telephone +(44) 1663 362888 +(1) 800-201-8822 Fax Not Available +(1) 800-708-9888 Website Not Available www.mgchemicals.com Email [email protected] [email protected] 1.4. Emergency telephone number Association / Organisation Verisk 3E (Access code: 335388) Not Available Emergency telephone numbers +(44) 20 35147487 Not Available Other emergency telephone +(0) 800 680 0425 Not Available numbers SECTION 2 HAZARDS IDENTIFICATION 2.1. Classification of the substance or mixture Classification according to regulation (EC) No 1272/2008 H319 - Eye Irritation Category 2, H317 - Skin Sensitizer Category 1, H334 - Respiratory Sensitizer Category 1 [CLP] [1] 1. Classified by Chemwatch; 2. Classification drawn from EC Directive 67/548/EEC - Annex I ; 3. -
United States Patent \ .J Patented Oct
2,907,738 United States Patent \ .j Patented Oct. 3, 1959 1 2 dibasic acids would also give polymerization in which the natural resin acid ester becomes an intimate part ‘ 2,907,738 of the ?nal polymer chemical composition. Such esteri ‘MIXED RESIN ACID ESTERS OF 4,4-BIS(47 ?cation reactions involving the phenolic hydroxyl groups HYDROXYARYL) PENTANOIC ACID 01 would conveniently be carried out by heating with a mix ture of the dibasic acid and acetic anhydride. Sylvan 0. Greenlee, Racine, Wis., assignor to The hydroxyaryl—substituted aliphatic acids contem~ S. C. Johnson & Son, Inc., Racine, Wis. plated for use in preparing the desired resinous poly No Drawing. Application June 30,1955 hydric phenols have two hydroxyphenyl groups attached ‘ Serial No.‘ 519,279’ 10 to a single carbon atom. The preparation of these sub~ stituted acids may be most conveniently carried out by 9 Claims. (Cl. 260-24)‘ condensing a keto-acid with the desired phenol. Expe rience in the preparation of bisphenols and related com pounds indicates that the carbonyl group of the keto This invention relates to new compositions which are 15 acid must be located next to a terminal carbon atom in ‘mixed esters of‘polyhydric alcohols, natural resin,acids, order to obtain satisfactory yields. A terminal carbon and hydroxyaryl-substituted aliphatic acids. atom as used herein refers to primary carbon atoms An object of this invention is to produce new com other ‘than the carboxyl carbon atom of the keto-acid. positions from natural resin acids, polyhydric alcohols Prior applications, Serial Nos. 464,607 and 489,300, and hydroxyaryl-substituted aliphatic acids which are 20 ?led October 25, 1954, and February 18, 1955, respec~ valuable as intermediates in the production of other more tively, disclose a number of illustrative compounds suit complex compositions. -
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(12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization llllllllllllllllllllllllllllllll^ International Bureau (10) International Publication Number (43) International Publication Date WO 2018/144996 Al 09 August 2018 (09.08.2018) WIPO I PCT (51) International Patent Classification: GHOSH, Souvik; c/o Manus Bio, Inc., 1030 Massachusetts C12N1/00 (2006.01) C12N15/00(2006.01) Avenue, Cambridge, MA 02138 (US). PIRIE, Christo C12N1/20 (2006.01) C12N15/52 (2006.01) pher; c/o Manus Bio, Inc., 1030 Massachusetts Avenue, C12N1/21 (2006.01) C12P 5/00 (2006.01) Cambridge, MA 02138 (US). DONAUD, Jason; c/o Manus C12N 9/00 (2006.01) Bio, Inc., 1030 Massachusetts Avenue, Cambridge, MA 02138 (US). UOVE, Aaron; c/o Manus Rio, Inc., 1030 (21) International Application Number: Massachusetts Avenue, Cambridge, MA 02138 (US). NAN, PCT/US2018/016848 Hong; c/o Manus Rio, Inc., 1030 Massachusetts Avenue, (22) International Filing Date: Cambridge, MA 02138 (US). TSENG, Hsien-chung; c/ 05 February 2018 (05.02.2018) o Manus Rio, Inc., 1030 Massachusetts Avenue, Cam bridge, MA 02138 (US). SANTOS, Christine Nicole, S.; (25) Filing Language: English c/o Manus Rio, Inc., 1030 Massachusetts Avenue, Cam (26) Publication Language: English bridge, MA 02138 (US). PHIUIPPE, Ryan; c/o Manus Rio, Inc., 1030 Massachusetts Avenue, Cambridge, MA 02138 (30) Priority Data: (US). 62/454,121 03 February 2017 (03.02.2017) US (74) Agent: HAYMAN, Mark, U. et al.; Morgan, Lewis & (71) Applicant: MANUS BIO, INC. [US/US]; 1030 Massachu Bockius LLP, 1111 Pennsylvania Avenue, NW, Washing setts Avenue, Cambridge, MA 02138 (US). -
Determination of Terpenoid Content in Pine by Organic Solvent Extraction and Fast-Gc Analysis
ORIGINAL RESEARCH published: 25 January 2016 doi: 10.3389/fenrg.2016.00002 Determination of Terpenoid Content in Pine by Organic Solvent Extraction and Fast-GC Analysis Anne E. Harman-Ware1* , Robert Sykes1 , Gary F. Peter2 and Mark Davis1 1 National Bioenergy Center, National Renewable Energy Laboratory, Golden, CO, USA, 2 School of Forest Resources and Conservation, University of Florida, Gainesville, FL, USA Terpenoids, naturally occurring compounds derived from isoprene units present in pine oleoresin, are a valuable source of chemicals used in solvents, fragrances, flavors, and have shown potential use as a biofuel. This paper describes a method to extract and analyze the terpenoids present in loblolly pine saplings and pine lighter wood. Various extraction solvents were tested over different times and temperatures. Samples were analyzed by pyrolysis-molecular beam mass spectrometry before and after extractions to monitor the extraction efficiency. The pyrolysis studies indicated that the optimal extraction method used a 1:1 hexane/acetone solvent system at 22°C for 1 h. Extracts from the hexane/acetone experiments were analyzed using a low thermal mass modular accelerated column heater for fast-GC/FID analysis. The most abundant terpenoids from Edited by: the pine samples were quantified, using standard curves, and included the monoter- Subba Rao Chaganti, University of Windsor, Canada penes, α- and β-pinene, camphene, and δ-carene. Sesquiterpenes analyzed included Reviewed by: caryophyllene, humulene, and α-bisabolene. Diterpenoid resin acids were quantified in Yu-Shen Cheng, derivatized extractions, including pimaric, isopimaric, levopimaric, palustric, dehydroabi- National Yunlin University of Science and Technology, Taiwan etic, abietic, and neoabietic acids. -
A Review of Wood Biomass-Based Fatty Acidsand Rosin Acids Use In
polymers Review A Review of Wood Biomass-Based Fatty Acids and Rosin Acids Use in Polymeric Materials Laima Vevere *, Anda Fridrihsone , Mikelis Kirpluks and Ugis Cabulis Polymer Department, Latvian State Institute of Wood Chemistry, 27 Dzerbenes Str., LV-1006 Riga, Latvia; [email protected] (A.F.); [email protected] (M.K.); [email protected] (U.C.) * Correspondence: [email protected]; Tel.: +371-28869638 Received: 26 October 2020; Accepted: 14 November 2020; Published: 16 November 2020 Abstract: In recent decades, vegetable oils as a potential replacement for petrochemical materials have been extensively studied. Tall oil (crude tall oil, distilled tall oil, tall oil fatty acids, and rosin acids) is a good source to be turned into polymeric materials. Unlike vegetable oils, tall oil is considered as lignocellulosic plant biomass waste and is considered to be the second-generation raw material, thus it is not competing with the food and feed chain. The main purpose of this review article is to identify in what kind of polymeric materials wood biomass-based fatty acids and rosin acids have been applied and their impact on the properties. Keywords: crude tall oil; tall oil; fatty acids; rosin acids; polymer materials 1. Introduction The success of plastics as a commodity has been significant and polymer materials are a part of everyday life. The advantages of polymers over other materials can be attributed to their adjustable properties, low cost and ease of processing. Worldwide, the manufacturing of polymers grows every year, reaching almost 360 million tonnes in 2018 [1]. In the light of environmental challenges of the 21st century, the development of novel low-cost and scalable monomers from renewable resources is essential. -
Tall Oil Production and Processing
TALL OIL PRODUCTION AND PROCESSING Tall oil is a mixture of mainly acidic compounds found, like turpentine, in pine trees and obtained as a by-product of the pulp and paper industry. It is used as a resin in many different industries, including mining, paper manufacture, paint manufacture and synthetic rubber manufacture. It is extracted at the pulp and paper mill, and undergoes the first two processing steps there. Step 1 - Extraction of tall oil soap The "black liquor" from the paper making process is concentrated and left to settle. The top layer is known as "tall oil soap", and is skimmed off. The rest is recycled for further use in paper making. Step2 - Production of crude tall oil The tall oil soap is reacted with acid to form crude tall oil. The following reaction occurs: + + R—COONa + H3O → R—COOH + H2O + Na The acids formed from this reaction, along with small quantities of other compounds of similar volatility, make up the crude tall oil. All crude tall oil produced in New Zealand is then sent to a plant in Mt. Maunganui to complete processing. Step 3 - Crude tall oil distillation The oil is distilled into five components with different boiling points: heads (which boils first), then fatty acids, distilled tall oil (a mixture of fatty and resin acids), resin acids (collectively known as rosin) and pitch (the residue). All of these can be used in various industries as is, but some of the rosin is also further processed on site. Step 4 - Production of rosin paper size "Paper size" is the substance that stops all paper from behaving like blotting paper. -
Resin Profile in a Bleached Kraft Pulp Process
Resin Profile in a Bleached Kraft Pulp Process Jennie Berglund May 2012 Degree Project in Polymeric Materials, First Level Department of Fibre and Polymer Technology Royal Institute of Technology Stockholm, Sweden Abstract The aim with this project was to investigate how the amount and composition of resins varied during the process producing bleached birch pulp at the mill SCA Packaging Munksund. A literature study about how the resin removal can be improved has also been included. Problems with resins in the process are common at pulp and paper mills, especially when birch is used as a raw material. The resin can cause deposits on the equipment leading to process stops, but also lowered mechanical properties and spots on the paper products. The addition of tall oil to the digester is one way of improving the removal of resins, seasoning of wood, and a good debarking are other ones. Also the different washing and bleaching steps can affect the amount of resin remaining in the pulp. In this study pulp samples from eight different positions in the process were analyzed. To extract the samples a Soxtec device was used. Results showed that the most effective resin removal happened during the washing in their first washing step after the digester, a DD-washer. Here 77 % of the resin was removed, of totally 88 % during the whole process. Another step which was effective was the final washing step, the PO-press. About 36 % of the remaining resins in the pulp which entered the PO-press were washed out here. The extracts were analyzed with GC-FID and GC-MS to identify and quantify the substances, and determine how the composition varied over the manufacturing process. -
Composition of American Distilled Tall Oils Thomas V
321 Composition of American Distilled Tall Oils Thomas V. Magee and Duane F. Zinkel* USDA Forest Service, Forest Products Laboratory, One Gifford Pinchot Drive, Madison, Wisconsin 53705-2398 The composition of the acidic components was deter mined for a cross section of distilled tall oil products pro duced in the United States. The composition varied wide ly as a result of different process designs and operations. Filtration of those products that crystallize offers a poten tial for upgrading some distilled tall oils. In the course of this work, a new resin acid, 7,15-pimaradien-18-oic acid, was isolated and identified. KEY WORDS: Distilled tall oil, resin acids, rosin, secodehydroabietate, tall oil. Tall oil is the most important domestic source of rosin and a major contributor to the production of fatty acids in the United States. Nearly all U.S. tall oil is distilled. The primary products are tall oil rosin (TOR) and tall oil fatty acids (TOFA); TOR and TOFA products are defined as contain ing a minimum of 90% resin acids or 90% fatty acids, respec tively. Other distillation cuts of mixed rosin and fatty acids not meeting this 90% minimum are grouped together as distilled tall oils. The yields and characteristics of TOR and TOFA depend on the design and operation of the distilla tion process, as does the byproduct distilled tall oil. The ob ject of this study was to characterize American distilled tall oils and to identify their principal components. 1 EXPERIMENTAL PROCEDURES = -28.8° (CHCl3; c 1.3); H nuclear magnetic resonance (NMR) (CDCl3): 0.83 (Me-20), 0.96 (Me-17), 1.25 (Me-19), Distilled tall oil samples were obtained from several tall 2.25 (dd, J = 1.7, 14.6 Hz, 1H, H-14), 3.64 (OMe), 4.96 (dd, oil fractionators.