Patent classifications
C08F4/44
Modifier, modified and conjugated diene-based polymer and rubber composition including the same
The present invention provides a modifier, a modified and conjugated diene-based polymer which is modified using the same, and a rubber composition including the modified and conjugated diene-based polymer, and more particularly, a modifier which includes a compound represented by Formula 1 and is capable of improving the mixing properties between a conjugated diene-based polymer and a filler, a modified and conjugated diene-based polymer which is modified using the same, and a rubber composition including the modified and conjugated diene-based polymer.
BLOCK COPOLYMER AND METHOD FOR PREPARING THE SAME
A block copolymer is disclosed. The block copolymer has a structure of formula (V) below:
[D].sub.x-[E].sub.y-[F].sub.z (V) wherein D, E, and F are each independently a compound of formula (VI) below, and D, E, and F are different from each other; and x, y, and z are each independently an integer from 1 to 40;
##STR00001## wherein A.sub.2 is O or S; R.sub.7 is H or a C.sub.1-6 alkyl; and R.sub.8 is a C.sub.1-12 alkyl, (CH.sub.2).sub.qN(R.sub.11).sub.2, CH.sub.2(CH.sub.2OCH.sub.2).sub.rCH.sub.2N(R.sub.12).sub.2, or CH.sub.2(CH.sub.2OCH.sub.2).sub.sCH.sub.2OR.sub.13, wherein R.sub.11, R.sub.12, and R.sub.13 are each independently a C.sub.1-6 alkyl; and q, r, and s are each independently an integer from 1 to 10.
BLOCK COPOLYMER AND METHOD FOR PREPARING THE SAME
A block copolymer is disclosed. The block copolymer has a structure of formula (V) below:
[D].sub.x-[E].sub.y-[F].sub.z (V) wherein D, E, and F are each independently a compound of formula (VI) below, and D, E, and F are different from each other; and x, y, and z are each independently an integer from 1 to 40;
##STR00001## wherein A.sub.2 is O or S; R.sub.7 is H or a C.sub.1-6 alkyl; and R.sub.8 is a C.sub.1-12 alkyl, (CH.sub.2).sub.qN(R.sub.11).sub.2, CH.sub.2(CH.sub.2OCH.sub.2).sub.rCH.sub.2N(R.sub.12).sub.2, or CH.sub.2(CH.sub.2OCH.sub.2).sub.sCH.sub.2OR.sub.13, wherein R.sub.11, R.sub.12, and R.sub.13 are each independently a C.sub.1-6 alkyl; and q, r, and s are each independently an integer from 1 to 10.
Method of preparing conjugated diene-based polymer by continuous polymerization
The present invention relates to a method of preparing a conjugated diene-based polymer by continuous polymerization using two or more reactors, and relates to a method of preparing a conjugated diene-based polymer which is capable of providing a conjugated diene-based polymer having improved Mooney viscosity and excellent cis 1,4 bond content and linearity, by controlling the injection amount of a conjugated diene-based monomer to each reactor in a specific ratio and resolving the deterioration phenomenon of physical properties, which might be generated in continuous reaction.
Block copolymer composition
A block copolymer composition is disclosed herein. In some embodiments, a block copolymer composition includes a diblock copolymer and a triblock copolymer, each including a polyolefin-based block and a polystyrene-based block, wherein the polyolefin-based blocks are present between 45 wt % to 90 wt %, wherein the polystyrene-based blocks are present between 10 wt % to 55 wt %, wherein the difference (ΔT) between a thermal decomposition initiation temperature and a thermal decomposition termination temperature (ΔT) measured by Thermo-Gravimetric Analysis (TGA) is 55° C. or greater, and the diblock copolymer and the triblock copolymer do not have a residual unsaturated bond.
Block copolymer composition
A block copolymer composition is disclosed herein. In some embodiments, a block copolymer composition includes a diblock copolymer and a triblock copolymer, each including a polyolefin-based block and a polystyrene-based block, wherein the polyolefin-based blocks are present between 45 wt % to 90 wt %, wherein the polystyrene-based blocks are present between 10 wt % to 55 wt %, wherein the difference (ΔT) between a thermal decomposition initiation temperature and a thermal decomposition termination temperature (ΔT) measured by Thermo-Gravimetric Analysis (TGA) is 55° C. or greater, and the diblock copolymer and the triblock copolymer do not have a residual unsaturated bond.
Method for producing an optoelectronic component and optoelectronic component
A method for producing an optoelectronic component and an optoelectronic component are disclosed. In an embodiment a method includes providing a semiconductor layer sequence comprising a plurality of pixels and an active layer, wherein the active layer is configured to emit a primary radiation in a blue region of an electromagnetic spectrum with a peak wavelength of between 420 nm inclusive and 480 nm inclusive, applying a first photoresist and a first converter material on the semiconductor layer sequence, exposing the first photoresist with radiation having the peak wavelength longer than the peak wavelength of the primary radiation, curing the first photoresist by polymerization in order to form a first converter layer comprising a matrix material and the first converter material and structuring the first converter layer.
Process for producing olefin terpolymers with bridged phenolate transition metal complexes
The present disclosure provides polymerization processes to produce polymeric materials, such as olefin terpolymers, using transition metal catalysts having bridged phenolate ligands. The polymerization process includes contacting a transition metal complex with a mixture olefin monomers that contain ethylene, propylene, and a cyclic diene to produce an olefin polymer and recovering the olefin polymer. The mixture of olefin monomers can include specified weight ratios for the various olefin monomers. The transition metal complex includes a bridged phenolate ligand bonded to a metal atom via covalent bonds by two oxygens, a coordinate covalent bond by a Group 15 atom, and a coordinate covalent bond by a Group 15 or 16 atom. The transition metal complex provides relatively high endocyclic alkene/vinyl selectivity to minimize hyperbranching during the production of olefin polymeric materials, such as EPDM and other terpolymers that are free or substantially free of gels.
Ziegler-Natta catalyst systems and methods of controlling particle size
A colloidal suspension includes an organic phase and a complex of Formula I as precursor for Ziegler-Natta catalyst synthesis:
XTiCl.sub.p(OR.sup.1).sub.4−p.Math.YMg(OR.sup.2).sub.q(OR.sup.3).sub.t (I).
In Formula I, a molar ratio of X to Y (X/Y) is from 0.2 to 5.0, p is 0 or 1, 0<q<2, 0<t<2, the sum of q and t is 2, R.sup.1, R.sup.2, and R.sup.3 are each independently a linear or branched alkyl, a linear or branched heteroalkyl, a cycloalkyl, a substituted cycloalkyl, a substituted heterocycloalkyl, a substituted aryl, or a (heteroaryl)alkyl; and R.sup.2 is not the same as R.sup.3.
Method for producing hydrogenated petroleum resin
Provided is a method for producing a hydrogenated petroleum resin having good compatibility with a base polymer and a good hue under a hydrogen pressure of 4 MPaG or less. A method for producing a hydrogenated petroleum resin, includes a hydrogenation step of hydrogenating a polymerization product of dicyclopentadiene and a vinyl aromatic compound in the presence of a catalyst, in which hydrogenation step is performed under conditions (A) to (C): (A) an amount of the catalyst used: 0.125 to 0.4 parts by mass relative to 100 parts by mass of a resin in the polymerization product, (V) a reaction pressure: 4 MPaG or less, and (C) a reaction temperature: 240° C. or higher.