Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F222/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides, or nitriles thereof
  • C08F222/30—Nitriles
  • C08F222/32—Alpha-cyano-acrylic acid; Esters thereof
  • C08F222/322—Alpha-cyano-acrylic acid ethyl ester, e.g. ethyl-2-cyanoacrylate
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D3/00—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
  • B05D3/002—Pretreatement
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D133/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
  • C09D133/04—Homopolymers or copolymers of esters
  • C09D133/14—Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
  • D01D5/00—Formation of filaments, threads, or the like
  • D01D5/0007—Electro-spinning
  • D01D5/0015—Electro-spinning characterised by the initial state of the material
  • D01D5/003—Electro-spinning characterised by the initial state of the material the material being a polymer solution or dispersion
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
  • D01D5/00—Formation of filaments, threads, or the like
  • D01D5/0007—Electro-spinning
  • D01D5/0061—Electro-spinning characterised by the electro-spinning apparatus
  • D01D5/0076—Electro-spinning characterised by the electro-spinning apparatus characterised by the collecting device, e.g. drum, wheel, endless belt, plate or grid
  • D01D5/0084—Coating by electro-spinning, i.e. the electro-spun fibres are not removed from the collecting device but remain integral with it, e.g. coating of prostheses
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
  • D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D01F6/16—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated carboxylic acids or unsaturated organic esters, e.g. polyacrylic esters, polyvinyl acetate
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
  • D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D01F6/18—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated nitriles, e.g. polyacrylonitrile, polyvinylidene cyanide

Definitions

• the present invention relates to a process for the production of micro- and nanofibres of poly(cyanoacrylate), to continuous, uniform coating layers obtained from said fibres and to substrates or articles provided with said coatings.
• polymer nanofibres which are characterized by their high surface area/volume ratio and by their mechanical properties, is of considerable interest in various applications such as the production of reinforced composites, of materials used as tissue scaffolds, as filter media and for controlled drug delivery.
• the main techniques for the production of polymer nanofibres comprise processes of extrusion of a polymer melt through holes of nanometric dimensions in a template and processes of electro spinning.
• Electro spinning involves the use of a source of high voltage for generating electrically charged polymer jets, which are collected on a substrate as a mat of nanofibres. This technique requires the polymer to be proces sable in the liquid state and to be able to withstand high voltage.
• fingerprints left on surfaces can act as sites of initiation for vapours of cyanoacrylate monomer and polymerization follows the thin lines of the fingerprints, forming poly(cyanoacrylate) fibres.
• main disadvantages of these approaches concern the difficulty of scale-up and lack of process control during moisture-activated polymerization, which leads to a crosslinked polymer structure that is in the form of a hard white solid.
• the general aim of the present invention is to provide a process that is simple, economical and rapid, and that can easily be implemented industrially, for producing micro- and nanofibres from cyanoacrylate monomers.
• a specific aim of the invention is to provide a process that allows large quantities of micro- and nanofibres to be produced by direct electro spinning from solutions.
• the invention relates to a process for the production of micro- and nanofibres of poly(cyanoacrylates), as defined in the accompanying claims, which form an integral part of the present description.
• the invention also relates to polymer coatings in the form of a uniform, continuous layer, obtained from the aforementioned micro- and nanofibres, as well as articles and/or substrates provided with said coating layers, as defined in the accompanying claims.
• the process according to the invention applies to any monomer of alkyl-2-cyanoacrylate (where alkyl can be Ci-C 8 ), among which the monomers that are the most representative and of greatest interest from the practical and industrial standpoint are methyl- or ethyl- or octyl- 2-cyanoacrylate and mixtures thereof.
• the first step of the process according to the invention envisages mixing the cyanoacrylate monomer in a dipolar aprotic solvent, including in particular dimethylformamide (DMF), dimethyl acetamide (DMAc), dimethyl sulphoxide (DMSO) and/or N-methyl-2- pyrrolidone (NMP); of these, DMSO is particularly preferred.
• the aforementioned dipolar aprotic solvent performs the dual function of solvent for the cyanoacrylate monomer and catalyst for initiating its polymerization, leading to the formation of a viscous gel of cyanoacrylate polymer or prepolymer.
• the cyanoacrylate monomer and the solvent can be mixed in any proportions by volume that lead to formation of the gel, for example with volume ratios from 0.1: 1 to 2: 1.
• DMSO generally it is preferable to mix equal volumes of cyanoacrylate monomer and DMSO; mixing can be carried out by drop wise addition of cyanoacrylate monomer to the dipolar aprotic solvent, for example contained in a glass test tube.
• the contents can be submitted to agitation to ensure complete mixing of the two liquids.
• the process that leads to formation of the gel as a result of contact of the cyanoacrylate monomer with the solvent is exothermic, therefore during formation of the gel it is preferable for the test tube or the container in question to be kept in a cold environment for the purpose of accelerating the exothermic gelling process.
• the gel After gelling, preferably the gel is left to equilibrate at room temperature.
• the second step of the process involves dissolution of the gel in a solvent, having properties suitable for electro spinning, which has properties of solvent for polyacrylates.
• Solvents suitable for the electro spinning process comprise acetonitrile, ketones, such as in particular acetone, chlorinated hydrocarbon solvents and simple Ci-C 4 carboxylic acids such as formic acid and acetic acid.
• ketones such as in particular acetone
• chlorinated hydrocarbon solvents such as formic acid and acetic acid.
• aqueous solvents, water, alcohols, and linear hydrocarbon solvents such as hexane and heptane, are not suitable.
• the preferred solvents are acetone and/or acetonitrile.
• the gel is dissolved using an amount of solvent suitable for obtaining a solution of poly(cyanoacrylate), suitable for electro spinning; typically, the gel is dissolved in the solvent in proportions from 1% to 30% w/v.
• Conventional electro spinning equipment comprises a syringe filled with the polymer solution, a syringe pump, a source of high voltage and a collector.
• the metal needle of the syringe typically has the function of electrode for inducing electric charges in the solution, under the influence of a strong electrostatic field.
• the diameters of the fibres can vary from a few nanometres to values above 5 ⁇ .
• the modified poly(cyanoacrylate) is characterized by excellent electro spinning properties, as the nanofibres obtained are long and of uniform diameter, without formation of porous or bead-like structures.
• nanofibres can easily be controlled by varying the concentration of the polymer in the solvent, without using surfactants or salts, which are required for other polymeric materials. Moreover, nanofibrous mats can be deposited over 2
• the main advantage of the process according to the invention is that the polymerization triggered by the dipolar aprotic solvent does not give rise to rapid polymerization with crosslinking, such as occurs with other initiators such as the amines. In these conditions, moisture does not cause rapid and irreversible polymerization, so that the cyanoacrylate polymerized (gelatinized) in this form is not thermosetting.
• the process allows a layer of nanofibres with controlled thickness and density to be deposited on various substrates, such as glass, metals and plastics.
• the fibres can be melted on the surfaces on which they are deposited, for example by thermal treatment in a stove, with a hot plate, with a microwave oven and/or laser, at a temperature between 100° and 300°C with treatment times typically between 10 seconds and 5 minutes, depending on the method of melting used and the thickness of the mat of fibres.
• Non- porous, transparent coatings are obtained that have good scratch resistance, antifriction properties that make them useful as lubricating coatings, hydrophilic self-cleaning properties and properties of non-condensation of water vapour (antifogging properties).
• This coating when applied to plastic substrates (for example of polydimethylsiloxane, PDMS), promotes the release of other polymeric materials (for example of the same PDMS) cured in situ on its surface (anti- sticking properties).
• plastic substrates for example of polydimethylsiloxane, PDMS
• PDMS polydimethylsiloxane
• This coating therefore also provides a process for the deposition of coatings, as an alternative to the vapour phase deposition of polymers; in particular, the exceptional properties of the coatings thus obtained cannot be achieved if the coatings are formed by other processes, such as spin-coating and casting.
• the cyanoacrylate coating developed also has good characteristics of biocompatibility, promoting cell growth more than the substrates conventionally used for these purposes (such as glass, polystyrene). Further features of the process according to the invention are illustrated by the embodiment example that follows.
• Figs. 1(a), (b) and (c) are photographs obtained with the scanning electron microscope (SEM), which illustrate the electrospun nanofibres at various magnifications:
• magnification x 1000 nanofibres obtained from 5% w/v solution of polymer in acetone
• magnification x 2000 nanofibres obtained from 10% w/v solution of polymer in acetone.
• a poly(cyanoacrylate) gel was prepared using ethyl-2-cyanoacrylate and dimethyl sulphoxide mixed in 1 : 1 ratio by volume, following the mixing procedure described above.
• Solutions of poly(cyanoacrylate) gel in acetone and acetonitrile were prepared with a concentration from 2% to 20% w/v. Each solution was collected in a 1-ml syringe fitted with a stainless steel needle with inside diameter of 0.5 mm, acting as spinneret, and connected to a generator of high voltage.
• the syringe was attached to a syringe pump for maintaining a flow rate of 3-5 ml/h, depending on the viscosity of the solution.
• a copper plate covered with aluminium foil was used as the collector.
• the voltage applied and the distance from the tip to the collector were 10-15 kV and 15 cm, respectively.
• the size of the fibres produced can be varied by acting upon the concentration of the polymer solution: an increased concentration of the solution greatly increases the solution viscosity, allowing fibres of larger diameter to be produced.
• the electrospun nanofibres thus obtained can be thermally treated in fusion (for example at a temperature of about 130°C) to form transparent coatings on glass substrates or on other surfaces, obtaining coatings with hydrophilic, self -cleaning properties.
• the coating obtained has high adherence to the substrate, antifriction and anti-scratch properties and hydrophilic behaviour with extremely low hysteresis, as well as anticondensation properties and biocompatibility.
• the invention thus provides a process that is economical, especially when using DMSO as catalyst, which is of low cost and does not require further purification relative to the grade that is commercially available.
• the fibres can be deposited on any surface, without requiring pretreatment or patterning; the polymer constituting the nanofibres and the coatings is biodegradable.
• the polymerization and electro spinning process proves to be suitable for allowing the incorporation of functional nanofillers in the fibres by direct dispersion or by means of precursors; that is, various natural or synthetic polymers can additionally be mixed in the nanofibres.
• the main application is the production of filters, membranes, biomedical scaffolds, medical devices, mechanical reinforcements, coatings, as well as applications in the textile industry.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Textile Engineering (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Mechanical Engineering (AREA)
• Organic Chemistry (AREA)
• Polymers & Plastics (AREA)
• Toxicology (AREA)
• Medicinal Chemistry (AREA)
• Wood Science & Technology (AREA)
• Materials Engineering (AREA)
• Life Sciences & Earth Sciences (AREA)
• Dispersion Chemistry (AREA)
• Artificial Filaments (AREA)
• Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
• Nonwoven Fabrics (AREA)
• Manufacture And Refinement Of Metals (AREA)

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• 2013
  • 2013-05-16 IT IT000396A patent/ITTO20130396A1/it unknown
• 2014
  • 2014-05-15 US US14/890,913 patent/US9624397B2/en active Active
  • 2014-05-15 CN CN201480026929.XA patent/CN105209509B/zh active Active
  • 2014-05-15 JP JP2016513486A patent/JP6368775B2/ja not_active Expired - Fee Related
  • 2014-05-15 EP EP14731050.2A patent/EP2997059B1/en active Active
  • 2014-05-15 WO PCT/IB2014/061457 patent/WO2014184761A1/en not_active Ceased

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