STATES PATENT OFFICE 2,454,047 CONVERSION of ALICYCLIC ALDEHYDES Harry Do V

Total Page:16

File Type:pdf, Size:1020Kb

STATES PATENT OFFICE 2,454,047 CONVERSION of ALICYCLIC ALDEHYDES Harry Do V Patented Nov. 16, 1948 2,454,047 UN STATES PATENT OFFICE 2,454,047 CONVERSION OF ALICYCLIC ALDEHYDES Harry do V. Finch, El Cerrito, Seaver A. Ballard, Orlnda, and Theodore W. Evans, Oakland, Calif., assignors to Shell Development Com pany, San Francisco, Calif., a corporation of t Delaware No Drawing. Application May 9, 1947, Serial'No. 747,128 20 Claims. (Cl. 260-514) i 2 . ., This invention relates to a process for the con aldehydes. The alcohols produced in the course version of alicyclic aldehydes, the production of of the present process, as hereinafter described, alicyclic acids and alcohols, and the production are of a new and useful variety. of aliphatic dicarboxylic acids. More particu The present invention provides an e?icient and larly, this invention provides a process whereby economical process for producing dicarboxylic alicyclic aldehydes may be converted simultane acids which obviates the objections to prior art ously to alicyclic acids and alcohols, and whereby processes, and which is especially adaptable to the.v the alicyclic acids so produced may be further commercial production thereof, and in the course acted upon to produce aliphatic dicarboxylic of which alicyclic acids and new and valuable acids. alicyclic alcohols are produced. I ‘ Certain reactions for the conversion of alde According to our invention, more fully de hydes to acids are well known, and various proc- ~ scribed hereinafter, an alicyclic aldehyde is con esses for these reactions have been described. tacted with a substantially anhydrous molten or However, these heretofore known reactions are "fused” alkali metal hydroxide, or mixture of two not generally applicable to alicyclic aldehydes, 25 or more alkali metal hydroxides. The resulting especially where the alicyclic aldehyde contains alkali metal carboxylate may or may not be sep one or more unsaturated linkages of ole?nic char arated from the reaction mixture. If separated. acter. between two nuclear carbon atoms, since it constitutes a valuable product which may be the necessary reagents or reaction conditions converted by methods known to the art to the commonly cause ring cleavage in such cases, corresponding acid if desired, or it may be further. thereby precluding formation of alicyclic acids, acted upon with an aqueous solution of an alka‘ and usually result in the formation of an aliphatic line material, as hereinafter fully described, to monocarboxylic acid. Accordingly, it is an object produce the salt of an aliphatic dicarboxylic acid. of the present invention to provide a process for This salt may be converted, also by methods the conversion of alicyclic aldehydes, and espe 25 known to the art, to the corresponding-acid if cially those alicyclic aldehydes having at least one desired. If the alkali metal carboxylate is not unsaturated linkage ofole?nic character between separated from the reaction mixture, the salt of ‘ two nuclear carbon atoms, to alicyclic acids. A a dlcarboxyllc acid, and subsequently the dicar further object is the production of alicycllc alco boxylic acid, may be prepared directly therefrom hols in the same step of the process. A further 80 by treating the reaction mixture with watenwlth object, is to react the alicyclic acids so produced adjustment of the concentration of the alkali if so that aliphatic dicarboxylic acids are produced. necessary and heating the resulting mixture, as A further object is to produce aliphatic dicar hereinafter described. The aliphatic dicar boxylic acids from alicyclic aldehydes without boxylic acid, prepared by either process, may be separating the intermediate alicyclic acid from 35 recovered by any convenient means, as by extrac the reaction mixture. tion of the acid salts with ether, acidi?cation with The aliphatic dicarboxylic acids produced ac hydrochloric acid, extraction of the acid with cording to the process of the present invention are ether, and evaporation of the ether. well known, and various methods for their prepa In carrying out the process of our invention we ration have been described. For example, have made the surprising discovery that, on con methods for the preparation of pimelic acid, a tacting an alicyclic aldehyde with a bath com- - typical dicarboxylic acid representative of those prising a. molten alkali metal hydroxide, or a mix herein contemplated which have been heretofore ture of such hydroxides, signi?cant yields of all described, include its preparation from penta cyclic alcohols are obtained. These alcohols may methylene dibromide through the cyanide proc 45 be separated from the reaction mixture,- which ess, and from trimethylene dibromide by means comprises chie?y the alkali metal carboxylate, of the malonic or acetoacetic ester synthesis. the desired alcohol, and unreacted alkali metal However, these methods are commonly suitable hydroxide, by dissolving the cooled reaction mix for laboratory scale preparation only, since the ture in, water,--acidifying with hydrochloric acid, cost of the reactants and the necessity for close 60 extracting with ether, and distlllating the ether control over the reaction conditions prevent sat extract. The acid and alcohol are separated by isfactory commercial scale operations. These the distillation. ' known processes for producing aliphatic dicar The initial reactants of the present invention‘, boxylic acids do not indicate that such acids alicyclic aldehydes, preferably have from 4 to 8 might successfully be prepared from alicyclic 55 carbon atoms in the nucleus or ring, though com-. s 2,464,047 3 4 pounds with larger rings may be used, and pref droxide baths should be operated in the lower erably the reactants have one double bond of region of the recited temperature limits. oleilnic character between two of the nuclear car In converting the alicyclic acid formed in the bon atoms, though alicyclic aldehydes with one or above-described step to the aliphatic dicarbox with two or even more such double bonds may be ylic acid, the acid and an aqueous solution of an employed and are within the scope of the present alkaline material are introduced into a vessel invention. The term "alicyclic," as used herein designed to withstand the pressure developed on with respect to aldehydes, acids and alcohols, is heating to the desired temperature, hereinafter meant to include those aldehydes, acids, and alco described. The proportions of acid, alkaline ma- hols which have a cyclic portion of aliphatic terial and water may be varied considerably, but character, and which may have one or more may advantageously be within the range of from double-bonds of ole?nic character between two about 0.5 to 2 mols of the acid, about 1.3 to 4 nuclear carbon atoms, but which excludes all mols of alkaline material and about 35 to 85 mols compounds having three conjugate double bonds of water. If the acid was not separated from the in a six membered ring, 1. e., compounds of aro 15 reaction mixture in the above-described step, the matic character. The alicyclic aldehyde react composition of the reaction mixture containing ants may be obtained from any convenient source. the alkali metal salt of the acid and free alkali For example, 3-cyclohexenecarboxaldehyde, used metal hydroxide may be adjusted usually by hereinafter to illustrate preferred embodiments adding water and, if necessary, an additional of the present invention, may be obtained by 20 quantity of an alkaline material, to bring the methods known to the art, as for example by composition substantially within the above re the addition reaction between butadiene and cited limits. In carrying out this step, we pre acrolein. fer to use an aqueous solution of an alkali metal In converting an alicyclic aldehyde to an all hydroxide. However, excellent results may be cyclic acid with simultaneous formation of an 25 achieved with aqueous solutions of other alkaline alicyclic alcohol, according to the process of our materials, such as the alkaline earth hydroxides, invention, the aldehyde is contacted with a molt e. g., barium hydroxide or ‘strontium hydroxide, en bath of any of the alkali metal hydroxides, or and aqueous solutions of salts of weal: acids and any mixture of said hydroxides, e. g., molten sodi strong bases, e. g., sodium phosphate. The reac um or potassium hydroxide, or a mixture thereof. 30 tion mixture is then heated under ambient pres We have found that molten mixtures of sodium sure, though higher or lower pressures may be and potassium hydroxides give excellent results, employed if desirable, to a temperature of from and the mixture may advantageously comprise 1 about 250° C. to about 450° C. In most instances mol of potassium hydroxide to 1/2 to 4 mols of temperatures of from about 280° C. to about 380° sodium hydroxide, which is the preferred range. C. give excellent results and are preferred. After Technical grade hydroxides may be used. since sufficient time for reaction has been allowed, we have found that the usual impurities do not usually from 2 to 10 hours, the dicarboxylic acid deleterlously a?ect the process. formed may be separated by any convenient _ In carrying out the process of our invention, we means. For example, the acid salt may be ex prefer to contact the aldehyde reactant with the tracted with ether, the ether extract acidified molten alkali metal hydroxide by passing the va with hydrochloric acid, the acid extracted with pors of the aldehyde into a bath of molten hydrox ether, and the ether evaporated. ide. However, other methods of contacting the al The products prepared according to the proc dehyde with the molten bath may be employed. ess of our invention have many uses. For ex For example, an aldehyde, and especially those 45 ample, the alicyclic acids may be treated to form aldehydes with a relatively high boiling point, esters, useful as plasticizers for various resins, may be contacted with the molten bath by intro the new alicyclic alcohols are useful as solvents, ducing the aldehyde in liquid form beneath or and form derivatives useful in detergent com upon the surface of the molten bath, in which positions, as emulsifying agents, and as driers in method the liquid may or mayinot be preheated 50 resins and varnishes, and the aliphatic dicar before contacting.
Recommended publications
  • (12) Patent Application Publication (10) Pub. No.: US 2015/0337275 A1 Pearlman Et Al
    US 20150337275A1 (19) United States (12) Patent Application Publication (10) Pub. No.: US 2015/0337275 A1 Pearlman et al. (43) Pub. Date: Nov. 26, 2015 (54) BOCONVERSION PROCESS FOR Publication Classification PRODUCING NYLON-7, NYLON-7.7 AND POLYESTERS (51) Int. C. CI2N 9/10 (2006.01) (71) Applicant: INVISTATECHNOLOGIES S.a.r.l., CI2P 7/40 (2006.01) St. Gallen (CH) CI2PI3/00 (2006.01) CI2PI3/04 (2006.01) (72) Inventors: Paul S. Pearlman, Thornton, PA (US); CI2P 13/02 (2006.01) Changlin Chen, Cleveland (GB); CI2N 9/16 (2006.01) Adriana L. Botes, Cleveland (GB); Alex CI2N 9/02 (2006.01) Van Eck Conradie, Cleveland (GB); CI2N 9/00 (2006.01) Benjamin D. Herzog, Wichita, KS (US) CI2P 7/44 (2006.01) CI2P I 7/10 (2006.01) (73) Assignee: INVISTATECHNOLOGIES S.a.r.l., (52) U.S. C. St. Gallen (CH) CPC. CI2N 9/13 (2013.01); C12P 7/44 (2013.01); CI2P 7/40 (2013.01); CI2P 13/005 (2013.01); (21) Appl. No.: 14/367,484 CI2P 17/10 (2013.01); CI2P 13/02 (2013.01); CI2N 9/16 (2013.01); CI2N 9/0008 (2013.01); (22) PCT Fled: Dec. 21, 2012 CI2N 9/93 (2013.01); CI2P I3/04 (2013.01); PCT NO.: PCT/US2012/071.472 CI2P 13/001 (2013.01); C12Y 102/0105 (86) (2013.01) S371 (c)(1), (2) Date: Jun. 20, 2014 (57) ABSTRACT Embodiments of the present invention relate to methods for Related U.S. Application Data the biosynthesis of di- or trifunctional C7 alkanes in the (60) Provisional application No.
    [Show full text]
  • Amt-10-1373-2017-Supplement.Pdf
    Supplement of Atmos. Meas. Tech., 10, 1373–1386, 2017 http://www.atmos-meas-tech.net/10/1373/2017/ doi:10.5194/amt-10-1373-2017-supplement © Author(s) 2017. CC Attribution 3.0 License. Supplement of New insights into atmospherically relevant reaction systems using direct analysis in real-time mass spectrometry (DART-MS) Yue Zhao et al. Correspondence to: Barbara J. Finlayson-Pitts (bjfi[email protected]) The copyright of individual parts of the supplement might differ from the CC-BY 3.0 licence. 31 1. Particle size distributions for amine-reacted diacids and -cedrene secondary organic 32 aerosol (SOA) particles. 33 1.1 Amine-reacted diacid particles. 34 At the exit of the flow reactor, size distributions of the amine-reacted diacid particles were 35 collected using a scanning mobility particle sizer (SMPS, TSI) consisting of an electrostatic 36 classifier (model 3080), a long differential mobility analyzer (DMA, model 3081) and a 37 condensation particle counter (model 3025A or 3776). Typical surface weighted size 38 distributions for (a) malonic acid (C3), (b) glutaric acid (C5), and (c) pimelic acid (C7) reacted 39 particles are presented in Fig. S1, with size distribution statistics given in Table S1. To reflect 40 the ~10% loss of amine-diacid particles in the denuder, a correction factor, Cf, of 1.1 was applied 41 when calculating the fraction of amine in the particles, fp. 3 (a) Malonic acid particles 1.6 (b) Glutaric acid particles ) ) w/o denuder -3 w/o denuder -3 w/ denuder w/ denuder cm cm 1.2 2 2 2 cm cm -4 -4 0.8 (10 (10 p p 1 0.4 dS/dlogD dS/dlogD 0 0.0 100 1000 100 1000 D (nm) D (nm) 42 p p 3 (c) Pimelic acid particles w/o denuder ) -3 w/ denuder Figure S1.
    [Show full text]
  • Production of Malonic Acid Through the Fermentation of Glucose
    University of Pennsylvania ScholarlyCommons Department of Chemical & Biomolecular Senior Design Reports (CBE) Engineering 4-20-2018 Production of Malonic Acid through the Fermentation of Glucose Emily P. Peters University of Pennsylvania, [email protected] Gabrielle J. Schlakman University of Pennsylvania, [email protected] Elise N. Yang University of Pennsylvania, [email protected] Follow this and additional works at: https://repository.upenn.edu/cbe_sdr Part of the Biochemical and Biomolecular Engineering Commons Peters, Emily P.; Schlakman, Gabrielle J.; and Yang, Elise N., "Production of Malonic Acid through the Fermentation of Glucose" (2018). Senior Design Reports (CBE). 107. https://repository.upenn.edu/cbe_sdr/107 This paper is posted at ScholarlyCommons. https://repository.upenn.edu/cbe_sdr/107 For more information, please contact [email protected]. Production of Malonic Acid through the Fermentation of Glucose Abstract The overall process to produce malonic acid has not drastically changed in the past 50 years. The current process is damaging to the environment and costly, requiring high market prices. Lygos, Inc., a lab in Berkeley, California, has published a patent describing a way to produce malonic acid through the biological fermentation of genetically modified easty cells. This proposed technology is appealing as it is both better for the environment and economically friendly. For the process discussed in this report, genetically modified Pichia Kudriavzevii yeast cells will be purchased from the Lygos lab along with the negotiation of exclusive licensing rights to the technology. The cells will be grown in fermentation vessels, while being constantly fed oxygen, glucose and fermentation media. The cells will excrete malonic acid in the 101 hour fermentation process.
    [Show full text]
  • Author's Response
    We thank the referees for their additional comments. We have revised the manuscript following the referees’ suggestions. You can find answers to the referee comments (in italics) below with additions to the manuscript and supplement text (in bold). Referee #1 The authors have provided responses to the questions, comments and issues pointed out by both referees. They have carried out 5 additional calculations and have modified the manuscript to account for suggested changes, where applicable. For this second round of reviews of this technical note, I will focus on the replies and manuscript sections with changes. Most of the issues raised in the first round have been addressed well. I have found a few issues to be further addressed before this manuscript is finalized for publication. The line numbers used in the following comments are those from the revised manuscript (ms version 3). 10 line 300: Regarding the acid dissociation reaction (R2) notation for oxalic acid, it is a bit odd that you write the reaction − + using HA for the acid, given that oxalic acid is a diacid. It would be better to write the reaction as H2A+H2O = HA +H3O and perhaps also list the second dissociation reaction involving HA− (even if not considered by COSMO-RS-DARE). Further along these lines, from the main text alone it remains unclear whether both acid dissociation reactions were considered in the 15 model or not; should be clarified. Author’s response: Thank you for this suggestion. We have added the second deprotonation reaction to the equilibrium reaction (R2). We also mention in the text why only the first deprotonation was considered.
    [Show full text]
  • United States Patent Office
    Patented Sept. 18, 1951 2568,426 UNITED STATES PATENT OFFICE 2,568,426 CONDENSATION PRODUCTS FROM POL ETHYLENC-UNSATURATED ALDEBY DE ADDUCTs, DERVATIVES THEREOF, AND METHODS FOR PRODUCING THE SAME Richard R. Whetstone, Orinda, William J. Raab, Berkeley, and Seaver A. Ballard, Orinda, Calif., assignors to Shell Development Company, San Francisco, Calif., a corporation of Delaware No Drawing. Application June 6, 1949, Serial No. 9,484 23 Claims. (C. 260-23) This invention relates to new compositions of present in the said adducts condense together matter and to methods for their preparation. to form an ester linkage. These novel condensas More particularly, the invention relates to novel tion products have been found to possess many condensation products prepared from adducts of unexpected beneficial properties which enable the unsaturated aldehydes and polyethylenic con said products to be utilized for many important pounds, to valuable derivatives prepared there industrial applications described hereinafter. from, and to methods for producing the same. The adducts utilized in the preparation of the Specifically, the invention provides new and novel condensation products comprise the re particularly useful condensation products which action products of alphabeta-ethylenically un are prepared by treating adducts of alpha,beta O saturated aldehydes and derivatives of polyethyl ethylenically unsaturated aldehydes and deriva enic acids. As used throughout the specification tives of polyethylenic acids with an ester-type and claims the expression "alphabeta-ethyleni condensation catalyst, such as aluminum isopro cally unsatured aldehydes' is meant to include poxide. The invention further provides valuable all those aldehydes having a formyl group at derivatives which may be prepared from the 5 tached to an aliphatic carbon atom which in above-described condensation products.
    [Show full text]
  • Certificate of Analysis
    National Institute of Standards and Technology Certificate of Analysis Standard Reference Material® 2277 Organic Acids in Methanol:Methylene Chloride This Standard Reference Material (SRM) is a solution of 24 organic acids in methanol:methylene chloride. This SRM is intended primarily for use in the calibration of chromatographic instrumentation used for the determination of organic acids. A unit of SRM 2277 consists of five 2 mL ampoules, each containing approximately 1.2 mL of solution. Certified Concentrations of Constituents: The certified concentration values and estimated uncertainties for the 24 constituents, expressed as mass fractions, are given in Table 1 along with the Chemical Abstract Service (CAS) Registry Numbers. The certified concentration values are based on results obtained from the gravimetric preparation of this solution and from the analytical results determined by using gas chromatography. A NIST certified value is a value for which NIST has the highest confidence in its accuracy in that all known or suspected sources of bias have been investigated or accounted for by NIST. Expiration of Certification: The certification of SRM 2277 is valid, within the measurement uncertainties specified, until 31 December 2017, provided the SRM is handled and stored in accordance with the instructions given in this certificate (see “Instructions for Use”). The certification is nullified if the SRM is damaged, contaminated, or otherwise modified. Maintenance of SRM Certification: NIST will monitor this SRM over the period of its certification. If substantive technical changes occur that affect the certification before the expiration of this certificate, NIST will notify the purchaser. Registration (see attached sheet) will facilitate notification.
    [Show full text]
  • Exploring Sources of Biogenic Secondary Organic Aerosol Compounds Using Chemical Analysis and the FLEXPART Model
    Atmos. Chem. Phys., 17, 11025–11040, 2017 https://doi.org/10.5194/acp-17-11025-2017 © Author(s) 2017. This work is distributed under the Creative Commons Attribution 3.0 License. Exploring sources of biogenic secondary organic aerosol compounds using chemical analysis and the FLEXPART model Johan Martinsson1,2, Guillaume Monteil3, Moa K. Sporre4, Anne Maria Kaldal Hansen5, Adam Kristensson1, Kristina Eriksson Stenström1, Erik Swietlicki1, and Marianne Glasius5 1Division of Nuclear Physics, Lund University, P.O. Box 118, 22100, Lund, Sweden 2Centre for Environmental and Climate Research, Lund University, Ecology Building, 22362, Lund, Sweden 3Department of Physical Geography, Lund University, Lund, P.O. Box 118, 22100, Lund, Sweden 4Department of Geosciences, University of Oslo, P.O. Box 1022, Blindern, 0315, Oslo, Norway 5Department of Chemistry and iNANO, Aarhus University, Langelandsgade 140, 8000, Aarhus C, Denmark Correspondence to: Johan Martinsson ([email protected]) Received: 1 February 2017 – Discussion started: 8 February 2017 Revised: 28 June 2017 – Accepted: 24 July 2017 – Published: 18 September 2017 Abstract. Molecular tracers in secondary organic aerosols 1 Introduction (SOAs) can provide information on origin of SOA, as well as regional scale processes involved in their formation. In Carbonaceous aerosols are abundant in ambient air around this study 9 carboxylic acids, 11 organosulfates (OSs) and the world and account for 40 % of the European PM2:5 mass 2 nitrooxy organosulfates (NOSs) were determined in daily (Putaud et al., 2010). The carbonaceous aerosol fraction has aerosol particle filter samples from Vavihill measurement severe effects on human health as well as a profound effect station in southern Sweden during June and July 2012.
    [Show full text]
  • Kinetic of Gas-Liquid Homogeneous Catalytic Oxidation of Cyclohexane Simone Gelosa, Davide Moscatelli, Davino Gelosa and Maurizio Masi Dept
    Kinetic of Gas-Liquid Homogeneous Catalytic Oxidation of Cyclohexane Simone Gelosa, Davide Moscatelli, Davino Gelosa and Maurizio Masi Dept. di Chimica, Materiali e Ingegneria Chimica “G. Natta” Politecnico di Milano Via Mancinelli 7 – 20131 Milano, Italy Adipic acid is an important industrial chemical product, principally used in nylon 66 production, synthetic resins and lubricants. Mostly, adipic acid is produced by a two step oxidation process of cyclohexane with air and nitric acid as oxidants (Reis, 1965; Danly and Campbell, 1978). Cyclohexane is initially oxidized with air at 150°-160°C to cyclohexanol and cyclohexanone. The latter two products are then converted to adipic acid by a further oxidation performed with nitric acid. The use of nitric acid is characterized by its high consumption and to serious corrosion problems. For these reasons, several studies were performed to extend the use of air as oxidizing agents also in the second step of the process (Reis, 1971; Tanaka, 1974; Rao and Raghunathan, 1984, 1986). In these processes the adipic acid synthesis is then performed in a single step, using acetic acid as solvent and cobalt, manganese or copper salts as catalyst. To reduce the induction time, particularly relevant in the considered reaction, and to obtain higher yields to adipic acid, the addition of a promoter is necessary. Most used promoters are aldehydes, cyclohexanol and cyclohexanone. The main reaction products are the dibasic acids as the adipic, the glutaric and the succinic acids. Recently, the reaction was studied also on a heterogenous catalysts, in particular on a cobalt catalyst supported on ion exchange resins (CoAPO-5) still operating with the main reactant diluted in acetic acid (Shen and Weng, 1988; Lin and Weng, 1993, 1994).
    [Show full text]
  • Identification of Methyl-Branched Chain Dicarboxylic Acids in Amniotic Fluid and Urine in Propionic and Methylmalonic Acidemia
    DICARBOXYLIC ACIDS IN AMNIOTIC FLUID 003 1-39981841181 I - 1 185$02.00/0 PEDIATRIC RESEARCH Vol. 18, No. 1 1, 1984 Copyright O 1984 International Pediatric Research Foundation, Inc Prinred in US.A. Identification of Methyl-branched Chain Dicarboxylic Acids in Amniotic Fluid and Urine in Propionic and Methylmalonic Acidemia CORNELIS JAKOBS, LAMBERTUS DORLAND, LAWRENCE SWEETMAN, MARINUS DURAN, WILLIAM L. NYHAN, AND SYBE K. WADMAN Department ofpediatricr, Academic Hospital of the Free University ofAmsterdarn, Amsterdam, The Netherlands [C.J.], University Children's Hospital "Het Wilhelmina Kinderziekenhuis, " Utrecht, The Netherlands [L.D.,M.D.,S.K.W.], and Department of Pediatrics, University of California Sun Diego, La Jolla, California 92093 [L.S.,W.L.N.] ABSTRACT. 3-Methyladipic, 4-methylpimelic, 4-meth- were considerably greater than in AF. Evidence was obtained for ylsuberic, pimelic, and azeleic acids were identified by gas the presence of a number of other methyl-branched dicarboxylic chromatography-mass spectrometry in the amniotic fluid acids. 4-MPA and 4-MSuA have not previously been identified of fetuses with propionic acidemia. These compounds were in body fluids. virtually undetectable in normal amniotic fluid. Concentra- tions much higher than those of the amniotic fluid were MATERIALS AND METHODS found in the urine of neonatal infants with propionic aci- demia and methylmalonic acidemia. It appears that the Normal AF samples were obtained between 16 and 18 weeks accumulation of these compounds is a consequence of the of pregnancy by amniocentesis and stored at -20°C. Amniotic accumulation of propionyl-CoA. Evidence was obtained for fluids from pregnancies at risk were sent for analysis as sterile the presence of other methyl-branched chain dicarboxylic fluids or frozen on dry ice and stored prior to analysis at -20°C.
    [Show full text]
  • Exploring Sources of Biogenic Secondary Organic Aerosol Compounds Using Chemical Analysis and the FLEXPART Model Johan Martinsson1,2, Guillaume Monteil3, Moa K
    Exploring sources of biogenic secondary organic aerosol compounds using chemical analysis and the FLEXPART model Johan Martinsson1,2, Guillaume Monteil3, Moa K. Sporre4, Anne Maria Kaldal Hansen5, Adam Kristensson1, Kristina Eriksson Stenström1, Erik Swietlicki1, Marianne Glasius5 5 1Division of Nuclear Physics, Lund University, Box 118, SE-22100, Lund, Sweden 2Centre for Environmental and Climate Research, Lund University, Ecology Building, SE-22362, Lund, Sweden 3Department of Physical Geography, Lund University, Lund, Box 118, SE-22100, Lund, Sweden 4Department of Geosciences, University of Oslo, Postboks 1022, Blindern, 0315, Oslo, Norway 5Department of Chemistry and iNANO, Aarhus University, Langelandsgade 140, DK-8000, Aarhus C, Denmark 10 Correspondence to: Johan Martinsson ([email protected]) Abstract. Molecular tracers in secondary organic aerosols (SOA) can provide information on origin of SOA, as well as regional scale processes involved in their formation. In this study nine carboxylic acids, eleven organosulfates (OSs) and two nitrooxy organosulfates (NOSs) were determined in daily aerosol particle filter samples from Vavihill measurement station in southern Sweden during June and July 2012. Several of the observed compounds are photo-oxidation products from 15 biogenic volatile organic compounds (BVOCs). Highest average mass concentrations were observed for carboxylic acids derived from fatty acids and monoterpenes (12.3±15.6 and 13.8±11.6 ng/m3, respectively). The FLEXPART model was used to link 9 specific surface types to single measured compounds. It was found that the surface category “sea and ocean” was dominating the air mass exposure (56%) but contributed to low mass concentration of observed chemical compounds. A principal component (PC) analysis identified four components, where the one with highest explanatory power (49%) 20 displayed clear impact of coniferous forest on measured mass concentration of a majority of the compounds.
    [Show full text]
  • Kent Academic Repository Full Text Document (Pdf)
    Kent Academic Repository Full text document (pdf) Citation for published version Ferris, Trevor John (2015) Zirconium-89 Complexes for Cell Tracking with Positron Emission Tomography. Doctor of Philosophy (PhD) thesis, University of Kent,. DOI Link to record in KAR https://kar.kent.ac.uk/48147/ Document Version UNSPECIFIED Copyright & reuse Content in the Kent Academic Repository is made available for research purposes. Unless otherwise stated all content is protected by copyright and in the absence of an open licence (eg Creative Commons), permissions for further reuse of content should be sought from the publisher, author or other copyright holder. Versions of research The version in the Kent Academic Repository may differ from the final published version. Users are advised to check http://kar.kent.ac.uk for the status of the paper. Users should always cite the published version of record. Enquiries For any further enquiries regarding the licence status of this document, please contact: [email protected] If you believe this document infringes copyright then please contact the KAR admin team with the take-down information provided at http://kar.kent.ac.uk/contact.html Zirconium-89 Complexes for Cell Tracking with Positron Emission Tomography Trevor John Ferris School of Physical Sciences, University of Kent at Canterbury A thesis is submitted to the University of Kent at Canterbury in partial fulfilment of the requirements for the degree of Doctor of Philosophy DECLARATION No part of this thesis has been submitted by me or anyone else in support of an application for any other degree or qualification at the University of Kent or at any other University.
    [Show full text]
  • Cyclohexane.Pdf
    Cyclohexane Cyclohexane is a cycloalkane with the molecular formula C H . 6 12 Cyclohexane Cyclohexane is non-polar. Cyclohexane is a colourless, flammable liquid with a distinctive detergent-like odor, reminiscent of cleaning products (in which it is sometimes used). Cyclohexane is mainly used for the industrial production of adipic acid and caprolactam, which are precursors to nylon.[5] Cyclohexyl (C6H11) is the alkyl substituent of cyclohexane and is abbreviated Cy.[6] Contents Production Modern production Names Historical methods Preferred IUPAC name Early failures Cyclohexane[2] Success Other names Reactions and uses Hexanaphthene (archaic)[1] Laboratory solvent and other niche uses Identifiers Conformation CAS Number 110-82-7 (http Solid phases s://commonche See also mistry.cas.org/d References etail?cas_rn=11 External links 0-82-7) 3D model (JSmol) Interactive image (https://ch Production emapps.stolaf.e du/jmol/jmol.ph p?model=C1CC Modern production CCC1) On an industrial scale, cyclohexane is produced by hydrogenation of 3DMet B04304 (http://w [7] benzene in the presence of a Raney nickel catalyst. Producers of ww.3dmet.dna.af cyclohexane account for approximately 11.4% of global demand for frc.go.jp/cgi/sho [8] benzene. The reaction is highly exothermic, with ΔH(500 K) = w_data.php?acc -216.37 kJ/mol). Dehydrogenation commenced noticeably above =B04304) 300 °C, reflecting the favorable entropy for dehydrogenation.[9] Beilstein 1900225 Reference ChEBI CHEBI:29005 (ht tps://www.ebi.ac. uk/chebi/searchI Historical methods d.do?chebiId=29 005) Unlike benzene, cyclohexane is not found in natural resources such ChEMBL ChEMBL15980 as coal.
    [Show full text]