Polyolefin/Thermoplastic Polyurethane Compositions

Total Page:16

File Type:pdf, Size:1020Kb

Polyolefin/Thermoplastic Polyurethane Compositions Europäisches Patentamt *EP000994919B1* (19) European Patent Office Office européen des brevets (11) EP 0 994 919 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.7: C08L 23/02 of the grant of the patent: // C08L23:02 23.06.2004 Bulletin 2004/26 (86) International application number: (21) Application number: 98942676.2 PCT/EP1998/004979 (22) Date of filing: 08.07.1998 (87) International publication number: WO 1999/002603 (21.01.1999 Gazette 1999/03) (54) POLYOLEFIN/THERMOPLASTIC POLYURETHANE COMPOSITIONS MADE FROM HYDROXY-TERMINATED POLYDIENE POLYMERS POLYOLEFIN/THERMOPLASTISCHE-POLYURETHANZUSAMMENSETZUNGEN AUS HYDROXYLENDGRUPPENHALTIGEN POLYDIENPOLYMEREN COMPOSITIONS DE POLYOLEFINE/POLYURETHANE THERMOPLASTIQUE PREPAREES A PARTIR DE POLYMERES DE POLYDIENE A TERMINAISON HYDROXY (84) Designated Contracting States: (72) Inventor: CENENS, Jozef, Lucien, Rudolf BE DE ES FR GB IT NL SE Sugar Land, TX 77478 (US) (30) Priority: 10.07.1997 US 52216 P (74) Representative: Kortekaas, Marcellinus C. J. A. et al (43) Date of publication of application: KRATON Polymers Research B.V., 26.04.2000 Bulletin 2000/17 P.O. Box 37666 1030 BH Amsterdam (NL) (73) Proprietor: KRATON Polymers Research B.V. 1031 CM Amsterdam (NL) (56) References cited: EP-A- 0 347 794 Note: Within nine months from the publication of the mention of the grant of the European patent, any person may give notice to the European Patent Office of opposition to the European patent granted. Notice of opposition shall be filed in a written reasoned statement. It shall not be deemed to have been filed until the opposition fee has been paid. (Art. 99(1) European Patent Convention). EP 0 994 919 B1 Printed by Jouve, 75001 PARIS (FR) EP 0 994 919 B1 Description [0001] This invention relates to thermoplastic polyurethane/polyolefin compositions. More specifically, the invention relates to compatible thermoplastic polyurethane/polyolefin compositions. 5 [0002] Thermoplastic Polyurethanes (TPU) are reaction products of 1) a polymeric diol, 2) a diisocyanate, and 3) a chain extender. The diol is usually either a polyether or a polyester of about 1000 to 4000 number average molecular weight. The diisocyanate used is commonly 4,4-diphenylmethane diisocyanate (MDI) but many other isocyanates may also be used. The chain extender is a low molecular weight diol, usually 1,4-butane diol (BDO), but in other work it has been found to be advantageous to use branched diols such as 2-ethyl-1,3-hexane diol (PEP). TPU's such as these 10 have been considered for use as additives to polypropylene to improve impact resistance and to improve adhesion of paint to the modified polypropylene. However, because of the polar nature of polyethers and polyesters, these con- ventional TPU's are too polar to be broadly compatible with polypropylene and other polyolefins and other non-polar polymers such as EPDM and butadiene and isoprene rubbers. This incompatibility is the reason why their blends frequently delaminate and therefore are not useful. From EP0347794A1 a thermoplastic resinous composition is known 15 that comprises a polyolefin, a thermoplastic polyurethane component and a compatibilizing amount of at least one modified polyolefin. This reference does not suggest how to obtain a polyolefin/thermoplastic polyurethane composition that is compatible without the need of a compatibilizer. The problem the present invention sets out to solve is to provide a compatible polyolefin/thermoplastic polyurethane composition. Such a composition has now surprisingly been found. [0003] Therefore, the present invention relates to a polyolefin/thermoplastic polyurethane composition which com- 20 prises: (a) from 99 to 80 percent by weight (%wt) of a polyolefin, and (b) from 1 to 20 %wt of a thermoplastic polyurethane composition having an OH/NCO molar ratio of 0.9 to 1.1 which is comprised of: 25 (1) from 90 to 40 %wt of a hydrogenated polydiene diol having a hydroxyl equivalent weight of 750 to 10,000, (2) from 5 to 50 %w of a diisocyanate, and (3) from 4 to 14 %wt of a chain extender having a functional group equivalent weight of from 30 to 300. 30 [0004] Hydroxy functional polydiene polymers (polydiene diols) are known. United States Patent No. 5,393,843 dis- closes that formulations containing these polymers, a melamine resin, and an acid catalyst can be cured by baking under normal bake conditions. This same patent also discloses that these polymers can be mixed with isocyanates to yield polyurethane compositions that cure at ambient temperature. It is known that, for instance, hydrogenated polyb- utadiene diols (EB diol) can be crosslinked by reaction with polyisocyanates at stoichiometry near 1/1 NCO/OH (NCO 35 represents the isocyanate functionality which is active in the crosslinking reaction and OH represents the hydroxyl functionality). [0005] The preferred polyolefins are polypropylene homopolymer and polypropylene copolymers containing at least 60 %wt of polymerized propylene units. [0006] The preferred polydiene diol is a hydrogenated polybutadiene diol. Preferably, the polydiene diol has a hy- 40 droxyl equivalent weight of 750 to 5000. [0007] The preferred chain extenders are alkyl-substituted aliphatic diols preferably C1-C8 alkyl-substituted aliphatic diols such as 2-ethyl-1,3-hexane diol (PEP diol), 2,2,4-trimethyl-1,3-pentane diol (TMPD diol), and 2-ethyl-2-butyl- 1,3-propane diol (BEPD diol). The aliphatic diol is preferably a C3-C50 aliphatic diol, more preferably a C3-C12 aliphatic diol. 45 [0008] Hydroxy functional polydiene polymers and other polymers containing ethylenic unsaturation can be prepared by copolymerizing one or more olefins, particularly diolefins, by themselves or with one or more alkenyl aromatic hy- drocarbon monomers. The copolymers may, of course, be random, tapered, block or a combination of these, as well as linear, radial or star. [0009] The hydroxy functional polydiene polymers may be prepared using anionic initiators or polymerization cata- 50 lysts. Such polymers may be prepared using bulk, solution or emulsion techniques. When polymerized to high molecular weight, the polymer will, generally, be recovered as a solid such as a crumb, a powder, or a pellet. When polymerized to low molecular weight, it may be recovered as a liquid such as in the present invention. [0010] In general, when solution anionic techniques are used, (co)polymers of conjugated diolefins, optionally with vinyl aromatic hydrocarbons, are prepared by contacting the monomer or monomers to be polymerized simultaneously 55 or sequentially with an anionic polymerization initiator such as group IA metals, their alkyls, amides, silanolates, naph- thalides, biphenyls or anthracenyl derivatives. It is preferred to use an organo alkali metal (such as sodium or potassium) compound in a suitable solvent at a temperature in the range from -150°Cto300°C, preferably at a temperature in the range from 0°Cto100°C. Particularly effective anionic polymerization initiators are organo lithium compounds having 2 EP 0 994 919 B1 the general formula: RLin 5 wherein R is an aliphatic, cycloaliphatic, aromatic or alkyl-substituted aromatic hydrocarbon radical having from 1 to about 20 carbon atoms and n is an integer of 1 to 4. [0011] Conjugated diolefins (dienes) which may be polymerized anionically include those conjugated diolefins con- taining from 4 to 24 carbon atoms such as 1,3-butadiene, isoprene, piperylene, methylpentadiene, phenyl-butadiene, 10 3,4-dimethyl-1,3-hexadiene, and 4,5-diethyl-1,3-octadiene. Isoprene and butadiene are the preferred conjugated diene monomers for use in the present invention because of their low cost and ready availability. Alkenyl (vinyl) aromatic hydrocarbons that may be copolymerized include vinyl aryl compounds such as styrene, various alkyl-substituted sty- renes, alkoxy-substituted styrenes, vinyl naphthalene and alkyl-substituted vinyl naphthalenes. [0012] The hydroxy functional polydiene polymers may have number average molecular weights of from 1500 to 15 20,000. Lower molecular weights require excessive crosslinking whereas higher molecular weights cause very high viscosity, making processing very difficult. Most preferably, the polymer is a predominately linear diol having a number average molecular weight of from 1500 to 10,000 (hydroxyl equivalent weight of 750 to 5000 because its a diol and has two hydroxyls) because this offers the best balance between the cost of the polymer, achieving good processing behavior, and achieving the right balance of mechanical properties in the final thermoplastic polyurethane. The average 20 functionality of the polydiene diol is preferably from 1.8 to 2.0, more preferably 1.9 to 2.0. [0013] Hydrogenated polybutadiene diols are preferred for use herein because they are easily prepared, they have low glass transition temperature, and they have excellent weatherability. The diols, dihydroxylated polydienes, are typically synthesized by anionic polymerization of conjugated diene hydrocarbon monomers with lithium initiators. This process is well known as described in U.S. Patents Nos. 4,039,593 and Re. 27,145. Polymerization commences with 25 a monolithium or dilithium initiator that builds a living polymer backbone at each lithium site. [0014] Polydiene diols used in this invention may be prepared anionically with a dilithium initiator such as described in United States Patents Nos. 5,391,663, 5,393,843, 5,405,911, and 5,416,168. The polydiene polymer can be made using a dilithium initiator, such as the compound formed by reaction of two moles of sec-butyllithium with one mole of diisopropenylbenzene. This diinitiator is typically used to polymerize a diene in a solvent typically composed of 90%wt 30 cyclohexane and 10%wt diethylether. The molar ratio of diinitiator to monomer determines the molecular weight of the polymer. The living polymer is then capped with two moles of ethylene oxide and terminated with two moles of methanol to yield the desired polydiene diol. [0015] Polydiene diol polymers can also be made using a mono-lithium initiator that contains a hydroxyl group which has been blocked as the silyl ether.
Recommended publications
  • Preparation of “Constrained Geometry” Titanium Complexes of [1,2]Azasilinane Framework for Ethylene/1-Octene Copolymerization
    molecules Article Preparation of “Constrained Geometry” Titanium Complexes of [1,2]Azasilinane Framework for Ethylene/1-Octene Copolymerization Seul Lee, Seung Soo Park, Jin Gu Kim, Chung Sol Kim and Bun Yeoul Lee * Department of Molecular Science and Technology, Ajou University, Suwon 443-749, Korea; [email protected] (S.L.); [email protected] (S.S.P.); [email protected] (J.G.K.); [email protected] (C.S.K.) * Correspondence: [email protected]; Tel.: +82-031-219-1844 Academic Editor: Kotohiro Nomura Received: 27 December 2016; Accepted: 7 February 2017; Published: 9 February 2017 5 t Abstract: The Me2Si-bridged ansa-Cp/amido half-metallocene, [Me2Si(η -Me4C5)(N Bu)]TiCl2, termed a “constrained-geometry catalyst (CGC)”, is a representative homogeneous Ziegler catalyst. CGC derivatives with the [1,2]azasilinane framework, in which the amide alkyl substituent is joined by the Si-bridge, were prepared, and the catalytic performances of these species was studied. Me4C5HSi(Me)(CH2CH=CH2)-NH(C(R)(R’)CH=CH2) (R, R’ = H or methyl; Me4C5H = tetramethylcyclopentadienyl) was susceptible to ring closure metathesis (RCM) when treated with Schrock’s Mo-catalyst to afford -Si(Me4C5H)(Me)CH2CH=CHC(R)(R’)NH- containing a six-membered ring framework. Using the precursors and the products of RCM, various CGC derivatives, i.e., 5 5 [-Si(η -Me4C5)(Me)CH2CH=CHC(R)(H)N-]TiMe2 (13, R = H; 15, R = Me), [-Si(η -Me4C5)(Me) 5 CH2CH2CH2CH2N]TiMe2 (14), [(η -Me4C5)Si(Me)(CH2CH=CH2)NCH2CH=CH2]TiMe2 (16), 5 5 [(η -Me4C5)Si (Me)(CH=CH2)NCH2CH=CH2]TiMe2 (17), and [(η -Me4C5)Si(Me)(CH2CH3)NCH2 CH2CH3]TiMe2 (18), were prepared.
    [Show full text]
  • Materials Properties Derived from INSITE Metallocene Catalysts
    REVIEW Materials Properties Derived from INSITE Metallocene Catalysts By P. Stephen Chum,* William J. Kruper, and Martin J. Guest Novel metallocene catalysts for the synthesis of ethylene/a-olefin copolymers are reviewed here. The technology usedÐsingle-site constrained geometry catalyst technologyÐis demonstrated to be useful for the preparation of a wide array of copolymers with unique materials properties, such as a high melt fracture resistance, as illustrated in the Figure. 1. General Aspects and Challenges of Catalysis procatalyst is inactive for olefin polymerization and may be activated through the use of Lewis acid catalysis with mixtures Over the past decade, the development of Dow's INSITE of modified methylalumoxane (MMAO) and electron-defi- (trademark of The Dow Chemical Co.) metallocene catalysts cient boranes such as tris-perfluorophenylborane (FAB). Al- has led to the launch of many new polyolefin product lines ternatively, the procatalyst may be activated through the use that had been previously unattainable from conventional of preformed, non-coordinating counterions, which are appro- Ziegler±Natta catalysis.[1] From a structure±activity perspec- priately ion-paired with protonated ammonium or trityl salts. IV tive, the catalyst ligand structures are readily tailored synthet- The nature of the catalytically active species derived from Ti ically from both an electronic and steric point of view. This analogues under polymerization conditions has recently been [4] alteration motif has led to the development and screening of reviewed. It is clear from our studies that variation of the several hundred ansa-cyclopentadienyl amido group IV metal Lewis acid components of the catalyst package can affect constrained-geometry catalysts (CGCs), which have been parameters such as efficiency, comonomer incorporation, Mw, evaluated for the preparation of a wide array of ethylene/ polydispersity, and more importantly, polymer microstructure a-olefin copolymers possessing unique materials properties.[2] and stereoregularity.
    [Show full text]
  • Polyolefin from Commodity to Specialty Mike Chung TC* Department of Materials Science and Engineering, Pennsylvania State University, University Park, PA 16802, USA
    cie al S nce ri s te & Mike Chung, J Material Sci Eng 2015, 4:2 a E M n f g DOI: 10.4172/2169-0022.1000e111 o i n l e a e n r r i n u g o Journal of Material Sciences & Engineering J ISSN: 2169-0022 EditorialResearch Article OpenOpen Access Access Polyolefin from Commodity to Specialty Mike Chung TC* Department of Materials Science and Engineering, Pennsylvania State University, University Park, PA 16802, USA Introduction the “Golden Age” of polymer science. The tremendous research efforts were generating the discovery of catalysts with superior activity and Polyolefins-including polyethylene (PE), polypropylene (PP), stereospecificity, as well as leading to economically viable production poly(1-butene), poly(4-methyl-1-pentene), ethylene-propylene elastomer processes and product developments. In the late 1970s, Kaminsky and (EPR), and ethylene-propylene-diene rubber (EPDM) - are the most Sinn discovered a new class of homogeneous (single-site) Ziegler-Natta widely used commercial polymers, with over 120 million metric tons catalyst, based on metallocene/methylaluminoxane (MAO), which global annual consumption, or close to 60% of the total polymer offers tremendous advantages in understanding the polymerization produced in year 2014. The popularity is due to their excellent mechanism and allows the design of catalyst to prepare new polymers combination of chemical and physical properties along with low (especially copolymers) with narrow molecular weight and composition cost, superior processability, and good recyclability. By controlling distributions. Polyolefin technology and industry have been changing crystallinity and molecular weight, polyolefins with a wide range of the landscape by broadening the monomer pool and introducing new thermal and mechanical properties have been produced for wide high performance products and new applications.
    [Show full text]
  • Copolymerization of Propylene with Higher Α-Olefins by A
    polymers Article Copolymerization of Propylene with Higher α-Olefins by a Pyridylamidohafnium Catalyst: An Effective Approach to Polypropylene-Based Elastomer Fei Yang 1, Xiaoyan Wang 2,*, Zhe Ma 1, Bin Wang 1,* , Li Pan 1 and Yuesheng Li 1 1 Tianjin Key Laboratory of Composite & Functional Materials, School of Materials Science and Engineering, Tianjin University, Tianjin 300350, China; [email protected] (F.Y.); [email protected] (Z.M.); [email protected] (L.P.); [email protected] (Y.L.) 2 State Key Laboratory of Organometallic Chemistry, Shanghai Institute of Organic Chemistry, Chinese Academy of Sciences, 345 Lingling Lu, Shanghai 200032, China * Correspondence: [email protected] (X.W.); [email protected] (B.W.) Received: 16 December 2019; Accepted: 1 January 2020; Published: 3 January 2020 Abstract: In this contribution, we explored the copolymerization of propylene with higher α-olefins, including 1-octene (C8) 1-dodecene (C12), 1-hexadecene (C16) and 1-eicosene (C20), by using a dimethyl pyridylamidohafnium catalyst. A series of copolymers with varied comonomer incorporation, high molecular weight and narrow molecular weight distribution were obtained at mild conditions. The effects of the insertion of the comonomers on the microstructure, thermal and final mechanical properties were systemically studied by 13C NMR, wide-angle X-ray scattering, DSC and tensile test. Excellent mechanical performances were achieved by tuning the incorporation and chain length of the higher α-olefins. When the comonomer content reached above 12 mol.%, polypropylene-based elastomers were obtained with high ductility. A combination of excellent elastic recovery and flexibility was achieved for the P/C16 copolymers with about 20 mol.% monomer incorporation.
    [Show full text]
  • US20100160506A1.Pdf
    US 2010.0160506A1 (19) United States (12) Patent Application Publication (10) Pub. No.: US 2010/0160506 A1 Wu et al. (43) Pub. Date: Jun. 24, 2010 (54) PRODUCTION OFSYNTHETIC Publication Classification HYDROCARBON FLUIDS, PLASTICIZERS (51) Int. Cl. AND SYNTHETICLUBRICANT BASE CSK 5/55 (2006.01) STOCKS FROM RENEWABLE FEEDSTOCKS CSK 5/109 (2006.01) C07D 30/03 (2006.01) (76) Inventors: Margaret May-Som Wu, Skillman, C07D 31 7/24 (2006.01) NJ (US); Karla Schall Colle, C07C I/207 (2006.01) Houston, TX (US); Ramzi Yanni (52) U.S. Cl. ......... 524/114; 524/280; 549/523: 549/229; Saleh, Baton Rouge, LA (US); 585/327 Allen D. Godwin, Seabrook, TX (57) ABSTRACT (US); John Edmond Randolph This disclosure is directed to an integrated method for making Stanat, Houston, TX (US) synthetic hydrocarbon fluids, plasticizers and polar synthetic lubricant base stocks from a renewable feedstock. More par Correspondence Address: ticularly, the disclosure is directed to a metathesis reaction of ExxonMobil Research & Engineering Company natural oil or its derivative ester and ethylene in the presence P.O. Box 900, 1545 Route 22 East of an effective amount of a metathesis catalyst to form linear Annandale, NJ 08801-0900 (US) alpha-olefins, internal olefins and reduced chain length trig lycerides. The linear alpha-olefins and/or internal olefins are polymerized to produce synthetic hydrocarbon fluids in the (21) Appl. No.: 12/633,742 presence of a suitable catalyst. The reduced chain length triglycerides are converted into polar synthetic lubricant base (22) Filed: Dec. 17, 2009 stocks or plasticizers by hydrogenation, isomerization, fol lowed by hydrogenations, or by hydroisomerization pro cesses.
    [Show full text]
  • Adhesive Bonding of Polyolefin Edward M
    White Paper Adhesives | Sealants | Tapes Adhesive Bonding of Polyolefin Edward M. Petrie | Omnexus, June 2013 Introduction Polyolefin polymers are used extensively in producing plastics and elastomers due to their excellent chemical and physical properties as well as their low price and easy processing. However, they are also one of the most difficult materials to bond with adhesives because of the wax-like nature of their surface. Advances have been made in bonding polyolefin based materials through improved surface preparation processes and the introduction of new adhesives that are capable of bonding to the polyolefin substrate without any surface pre-treatment. Adhesion promoters for polyolefins are also available that can be applied to the part prior to bonding similar to a primer. Polyolefin parts can be assembled via many methods such as adhesive bonding, heat sealing, vibration welding, etc. However, adhesive bonding provides unique benefits in assembling polyolefin parts such as the ability to seal and provide a high degree of joint strength without heating the substrate. This article will review the reasons why polyolefin substrates are so difficult to bond and the various methods that can be used to make the task easier and more reliable. Polyolefins and their Surface Characteristics Polyolefins represent a large group of polymers that are extremely inert chemically. Because of their excellent chemical resistance, polyolefins are impossible to join by solvent cementing. Polyolefins also exhibit lower heat resistance than most other thermoplastics, and as a result thermal methods of assembly such as heat welding can result in distortion and other problems. The most well-known polyolefins are polyethylene and polypropylene, but there are other specialty types such as polymethylpentene (high temperature properties) and ethylene propylene diene monomer (elastomeric properties).
    [Show full text]
  • Light Linear Alpha Olefin Market Study
    Light Linear Alpha Olefin Market Study Chemical Strategic Report Prospectus Light Linear Alpha Olefin Market Study Light Linear Alpha Ole n Market Study Light Linear Alpha Ole n Market Study Contents Introduction The linear alpha olefin (“LAO”) business is complex, serving a broad range of industries and Introduction ............................................................................................. 3 applications therein from commodity plastics to small volume fine and performance chemicals. Study Scope ............................................................................................. 5 A simplified map of the LAO value chain is given below: Key Questions Addressed in the Study ............................................... 7 Deliverables .............................................................................................. 8 Alpha Olefins Supply Chain Proposed Table of Contents ................................................................. 9 Full Range Ethylene Polybutene-1 Processes Butene-1 Methodology .......................................................................................... 11 PE/PP Hexene-1 Study Team ............................................................................................ 15 Comnomer Dimerization Plasticizer Alcohols Qualifications ......................................................................................... 18 Octene-1 Polyolefin Elastomers Trimerization About Chemical at IHS Markit ............................................................. 21
    [Show full text]
  • Licensed Technologies Innovative | Proven | Value-Adding
    Licensed Technologies Innovative | Proven | Value-adding lyondellbasell.com Saudi Ethylene and Polyethylene Company (SEPC), Al-Jubail Industrial City, Kingdom of Saudi Arabia LyondellBasell is the world’s third-largest independent chemical company. We have annual revenues of approximately $30.8 billion and more than 14,000 employees worldwide. Our vertically integrated facilities, broad product portfolio, manufacturing flexibility, superior technology base and reputation for operational excellence enable us to deliver exceptional value to our customers across the petrochemical chain – from refining to advanced product applications. Product diversity and vertical integration allow LyondellBasell to capture value at every step of the petrochemical chain. Natural Gas Wellhead Crude Liquids Capturing value along the chain Refining Refining Fuels Olefins Olefins Crackers Olefins Aromatics T echnology Propylene Olefin OxyFuels Polyethylene Polypropylene Polybutene-1 Acetyls Ethylene Oxide Styrene Derivatives Oxide Glycols, Glycol Ethers Glycols 2nd Level PP Catalloy Derivatives Compounding Butanediol Glycol Ethers Refining & OxyFuels Olefins & Polyolefins Olefins & Polyolefins Intermediates & Derivatives Technology Americas Europe, Asia & International 2 A global leader in polyolefins and chemicals technology, production and marketing About LyondellBasell LyondellBasell’s technologies are some of the Global capacity positions most reliable, efficient and cost effective in the With major administrative offices in Houston, world. With over 280 licensed
    [Show full text]
  • Development of Constrained Geometry Complexes of Group 4
    A Dissertation entitled Development of Constrained Geometry Complexes of Group 4 and 5 Metals by Ryan Thomas Rondo Submitted to the Graduate Faculty as a partial fulfillment of the requirements for the Doctor of Philosophy Degree in Chemistry Dr. Mark R. Mason, Committee Chair Dr. Patricia Komuniecki, Dean College of Graduate Studies The University of Toledo May 2010 An abstract of Development of Constrained Geometry Complexes of Group 4 and 5 Metals Ryan Thomas Rondo Submitted to the Graduate Faculty in partial fulfillment of the requirements for the Doctor of Philosophy Degree in Chemistry The University of Toledo May 2010 Constrained geometry catalysts (CGC) are known to be active in the polymerization and copolymerization of alkenes with a distinct control over polymer tacticity. The tethering of one 5-cyclopentadienyl moiety and one pendant donor gives these compounds an accessible metal center as well as ability to maintain their structure throughout the catalytic process. Complexes of this type typically feature one pendant amido donor. Replacement of the pendant amido donor with a nitrogen heterocycle such as an indolyl- or pyrrolyl-group should result in electrophilic metal centers due to reduced N M donation, a consequence of electron delocalization of the nitrogen lone pair in the aromatic system. This dissertation reports the development of a new series of constrained geometry ligands that feature indolyl- and pyrrolyl- donor moieties. iii In chapter 2, the synthesis and characterization of a series of acetal precursors and their corresponding di(3-methylindolyl)ethane and dipyrrolylethane constrained geometry ligands is reported. Within this report are two new acetal precursors, fluorenyl acetaldehyde diethylacetal, and indenyl acetaldehyde diethylacetal.
    [Show full text]
  • Monomer Recovery in Polyolefin Plants
    PETROCHEMICALSand GAS PROCESSING Monomer recovery in polyolefin plants This article outlines the application in polyolefin plants of a membrane based process, VaporSep, for separating and recovering hydrocarbons from nitrogen - in particular, the treatment of resin degassing vent streams Marc L Jacobs DouglasE Gottschlich Richard W Baker MembraneTechnology & ResearchInc (MTR) hemical feedstocks, or monomers, such as ethylene and propylene, Selective are the single largest operating + cost in the manufacture of polyolefins. Layer Due to the intensely competitive nature of the industry, monomer losses in vent streams are a mqjor concern for produc- Microporous ers. Typical losses for a plant range from <_ 1 to 2 per cent of the feed and can Layer account for 2000 to 4000 tons/year of lost monomer. Assuming a cost of $350/ton, these vent streams represent a significant opportunity for recovery and Support recycling of raw materials web A membrane-based process called 'l VaporSep, to separate and recover Figure The three-layer VoporStepmembrqne hydrocarbons and nitrogen in poly- olefin plants, has been developed by free selective layer which performs the and parallel flow combinations to MTR. The process is based on a poly- separation. meet the requirements of a particular meric membrane that selectively perme- After manufacture as flat sheet, the application. ates hydrocarbons, compared to light membrane is packaged into a spiral- gases such as nitrogen and hydrogen. wound module, as shown in Figure 2. Resin degassing vent streams This article describes how the process is The feed gas enters the module and In a typical polyolefin plant, propylene, applied to resin degassing vent streams flows between the membrane sheets.
    [Show full text]
  • Self-Healing Polymeric Materials: a Review of Recent Developments
    ARTICLE IN PRESS Prog. Polym. Sci. 33 (2008) 479–522 www.elsevier.com/locate/ppolysci Self-healing polymeric materials: A review of recent developments Dong Yang WuÃ, Sam Meure, David Solomon CSIRO Manufacturing and Materials Technology, Gate 5, Normanby Road, Clayton South, Victoria 3168, Melbourne, Australia Received 17 June 2007; received in revised form 30 January 2008; accepted 18 February 2008 Available online 4 March 2008 Abstract The development and characterization of self-healing synthetic polymeric materials have been inspired by biological systems in which damage triggers an autonomic healing response. This is an emerging and fascinating area of research that could significantly extend the working life and safety of the polymeric components for a broad range of applications. An overview of various self-healing concepts for polymeric materials published over the last 15 years is presented in this paper. Fracture mechanics of polymeric materials and traditional methods of repairing damages in these materials are described to provide context for the topic. This paper also examines the different approaches proposed to prepare and characterize the self-healing systems, the different methods for evaluating self-healing efficiencies, and the applicability of these concepts to composites and structural components. Finally, the challenges and future research opportunities are highlighted. Crown Copyright r 2008 Published by Elsevier Ltd. All rights reserved. Keywords: Polymeric materials; Self-healing; Composite repair; Biomimetic repair Contents 1. Introduction . 480 2. Fracture mechanics of polymeric materials. 483 3. Traditional repair methods for polymeric materials. 485 3.1. Repair of advanced composites . 485 3.1.1. Welding . 485 3.1.2.
    [Show full text]
  • Globally Established Polyolefin Plants
    Globally established polyolefin plants. Competence in PE and PP projects opens markets. 02 Linde Engineering: Polyolefin plants Linde Engineering: Polyolefin plants 03 Knowing what makes the market tick. We’re familiar with the processes for PP and PE – worldwide. Polyethylene (PE) and polypropylene (PP) belong to the Integrating petrochemical complexes polymers with the highest demand and growth rates world- wide. More than 50 % of all ethylene produced is consumed Very few companies have the know-how to build turnkey in polymerisation processes for the production of PE and PP. integrated petrochemical complexes. Linde is in a unique More than 30 years of experience in the polyethylene and position of being able to offer a complete spectrum of polypropylene market have given Linde a profound knowl- technologies along the olefin/polyolefin chain, such as edge base in both engineering and project execution for gas separation, ethylene, propane dehydration, poly- such plants. ethylene and polypropylene, linear alpha olefins. Our experience of having constructed PE and PP plants in numerous countries around the world gives us, Linde, the capability to focus on the planning and project develop- ment required to provide a truly successful turnkey plant. One-stop individual support We offer the full range of engineering services for poly- ethylene and polypropylene projects, including: 3 Consulting services 3 Project development 3 Economical and technical feasibility studies 3 Licensing arrangements 3 Financing 3 Arrangement of premarketing and off-take 3 Support and documentation for authority engineering 3 Project management 3 Engineering and design 3 Procurement 3 Construction 3 Commissioning and start-up 3 Training of operational and maintenance personnel 3 After-sales support 04 Linde Engineering: Polyolefin plants Working hand in hand.
    [Show full text]