Study of Methods for Processing Tall Oil. Frank Abel Anderson Louisiana State University and Agricultural & Mechanical College
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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. -
The Miracle Resource Eco-Link
Since 1989 Eco-Link Linking Social, Economic, and Ecological Issues The Miracle Resource Volume 14, Number 1 In the children’s book “The Giving Tree” by Shel Silverstein the main character is shown to beneÞ t in several ways from the generosity of one tree. The tree is a source of recreation, commodities, and solace. In this parable of giving, one is impressed by the wealth that a simple tree has to offer people: shade, food, lumber, comfort. And if we look beyond the wealth of a single tree to the benefits that we derive from entire forests one cannot help but be impressed by the bounty unmatched by any other natural resource in the world. That’s why trees are called the miracle resource. The forest is a factory where trees manufacture wood using energy from the sun, water and nutrients from the soil, and carbon dioxide from the atmosphere. In healthy growing forests, trees produce pure oxygen for us to breathe. Forests also provide clean air and water, wildlife habitat, and recreation opportunities to renew our spirits. Forests, trees, and wood have always been essential to civilization. In ancient Mesopotamia (now Iraq), the value of wood was equal to that of precious gems, stones, and metals. In Mycenaean Greece, wood was used to feed the great bronze furnaces that forged Greek culture. Rome’s monetary system was based on silver which required huge quantities of wood to convert ore into metal. For thousands of years, wood has been used for weapons and ships of war. Nations rose and fell based on their use and misuse of the forest resource. -
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. -
( 12 ) United States Patent
US009902815B2 (12 ) United States Patent ( 10 ) Patent No. : US 9 ,902 , 815 B2 Tamminen et al. ( 45 ) Date of Patent: Feb . 27 , 2018 ( 54 ) FUNCTIONALIZED LIGNIN AND METHOD ( 58 ) Field of Classification Search OF PRODUCING THE SAME ??? . .. C07G 1 / 00 See application file for complete search history . @(71 ) Applicant : Teknologian tutkimuskeskus VTT , VTT (FI ) ( 56 ) References Cited U . S . PATENT DOCUMENTS @(72 ) Inventors : Tarja Tamminen , Espoo (FI ) ; Jarmo Ropponen , Espoo (FI ) ; Eva - Lena Hult , 2 ,429 , 102 A 10 / 1947 Lewis et al. Espoo ( FI) ; Kristiina Poppius- Levlin , 3 , 149 , 085 A 9 / 1964 Ball et al . Espoo (FI ) 4 ,017 ,430 A * 4 / 1977 Briggs .. .. .. 530 / 502 5 ,773 , 590 A * 6 / 1998 Hart 530 / 500 6 ,172 ,204 B1 * 1 /2001 Sarkanen et al. 530 /500 @(73 ) Assignee : Teknologian tutkimuskeskus VTT Oy, 2010 /0105798 A1 * 4 /2010 Hasegawa . .. .. 522 / 99 Espoo (FI ) 2010 /0152428 A1* 6 / 2010 Gifford et al . .. .. .. 530 / 504 2010 / 0204368 A1 * 8 / 2010 Benko et al. .. .. .. .. .. .. .. 524 / 73 ( * ) Notice : Subject to any disclaimer, the term of this 2010 / 0331531 A1 * 12 / 2010 Mykytka .. .. 530 / 501 patent is extended or adjusted under 35 2011/ 0263836 A1 * 10 / 2011 Vuorenpalo et al. .. .. 530 / 500 U . S . C . 154 ( b ) by 33 days. 2012 /0012035 A1 * 1 / 2012 Blank et al. .. .. 106 / 802 ( 21) Appl. No. : 14 /348 , 904 OTHER PUBLICATIONS (22 ) PCT Filed : Oct. 8 , 2012 Holmbom ( Journal of the American Oil Chemists Society , 1977 , p . 289 - 293 ) . * Stenberg et al . (Surface Coatings International Part B : Coatings ( 86 ) PCT No. : PCT/ FI2012 /050965 Transactions , vol. 88 , B2 , 83 - 156 , 2005 ) . -
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. -
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. -
What's a Tree Done for You Lately?
What’s a Tree Done For You Lately? Some common products we get from trees and how they are made Scott Leavengood Director, Oregon Wood Innovation Center, Oregon State University This publication is on-line at http://owic.oregons tate.edu/teachers.php Introduction Products from trees are all around us. Some items are easy to recognize as products we get from trees - This publication will serve as valuable lumber, plywood, and paper, for example. Other background material for several activities in the items such as cellophane, a rayon scarf, and a Project Learning Tree (PLT) Pre K-8 chocolate bar, may not be as easy to recognize as a Environmental Education Activity Guide (1993, product from trees. American Forest Foundation, Washington, D.C.). In particular, the publication is well- This publication will help educators teach students suited to activities 12 and 13, Tree Treasures, about the variety of products we obtain from trees and We All Need Trees, respectively. and how the products are made. It serves as a reference for anyone who wants to know more Number 12 - Tree Treasures about products we obtain from trees. Objectives: 1) identify and categorize products derived from Products from trees may be categorized as: trees, 2) find out which forest products are recyclable • products from wood fiber - for example, paper or reusable, and products and purified cellulose products (rayon, 3) recommend actions for conserving forest cellophane, food additives, and resources. pharmaceuticals); Number 13 - We All Need Trees • products derived -
Tall Oil Soap Recovery TAPPI Kraft Recovery Short Course
Tall Oil Soap Recovery TAPPI Kraft Recovery Short Course C.D. Foran, Arizona Chemical Co., Savannah GA Slide 1 Tall oil soap is a mixture of the sodium salts of rosin acids, fatty acids and neutrals that separates from kraft black liquor. Composition of Crude Tall Oil Northern New Southern USA & Zealand & USA Canada Scandinavia Chile Acid Number 165 135 132 158 Resin Acids % 41 30 23 43 Fatty Acids % 51 55 57 40 Neutrals % 8 15 20 14 1 Slide 2 How Much Tall Oil Can Be Recovered ? Soap Recovery Tall Oil Tall Oil 52 26 51 25.5 kg/1000 kg lb/ ODT Region 50 25 OD Wood Wood 49 24.5 Piedmont 24 48 48 24 47 23.5 kg CTO/ODt Pine Wood Pine CTO/ODt kg Coastal 26 52 Lb. CTO/ODT Pine Wood46 23 45 22.5 Canada 11.5 23 Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec Average Southwestern 31.5 63 Impact of Storage Time on West of 7.5 15 Tall Oil Loss 100% Cascades 80% 60% NZ & Chile 12 24 40% Tall Oil Loss Tall Finland 18.5 37 20% 0% 0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 Sweden 25 50 Storage Time (weeks) Outside Chips Roundwood Chips Slide 3 Why Should Tall Oil Soap Be Recovered ? •To improve pulp and paper mill operations •To reduce the toxicity of pulp mill effluents, •To reduce accidents due to slips and falls. •To increase mill revenue 2 Slide 4 Tall Oil Soap Should Be Recovered To Improve Pulp and Paper Mill Operations : Impact of Improved Soap Removal on Evaporator Overall Heat Transfer 1. -
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.