Provided is a continuous production apparatus and a continuous production method capable of preventing the countercurrent of evaporation components generated at the time of polymerization so that continuous solution polymerization reactions can progress reliably. A continuous production apparatus (100) includes a housing chamber (2) configured to house a plurality of reaction vessels (1a to 1d); wherein a reaction mixture is formed by subjecting monomers to a polymerization reaction in a solvent in at least one of the reaction vessels; the reaction vessels communicate with one another via a gas phase part (4); the reaction vessels are sequentially connected; the reaction mixture successively moves to each of the reaction vessels; and the housing chamber includes a baffle (9) configured to narrow the cross-sectional area of the gas phase part at the boundary between at least one pair of adjacent reaction vessels or in the vicinity of the boundary.

A composition includes a compound represented by Formula (1) and a pigment. In Formula (1), R.sup.1 represents an (m+n)-valent linking group, P.sup.1 represents a polymer chain which has a polyester repeating unit in a main chain, and of which a weight-average molecular weight is 1000 or more, P.sup.2 represents a polymer chain which is different from P.sup.1 and has a repeating unit derived from a monomer having an ethylenically unsaturated bonding group in a main chain, m represents a number of 1 to 9, n represents a number of 1 to 9, and m+n satisfies 4 to 18.

##STR00001##

The invention relates to a method for producing a polymer comprising the following steps: (A) depositing a radically cross-linkable resin, obtaining a radically cross-linked resin; and (B) treating the radically cross-linked resin under conditions which are sufficient to trigger a chemical reaction that is different from the radical cross-linking in the radically cross-linked resin. The radically cross-linkable resin comprises a curable component, in which there are NCO groups, olefinic CC double bonds and epoxide groups, and the chemical reaction in the radically cross-linked resin that is different from the radical cross-linking is the reaction of NCO groups and epoxide groups to form oxazolidinone groups.

The present invention provides an organometal catalyst having a cationic transition metal complex and a borate-based bulky anion, a method for preparing the same, and a method for preparing an oligomer using the same.

Provided is a continuous production apparatus and a continuous production method capable of preventing the countercurrent of evaporation components generated at the time of polymerization so that continuous solution polymerization reactions can progress reliably. A continuous production apparatus (100) includes a housing chamber (2) configured to house a plurality of reaction vessels (1a to 1d); wherein a reaction mixture is formed by subjecting monomers to a polymerization reaction in a solvent in at least one of the reaction vessels; the reaction vessels communicate with one another via a gas phase part (4); the reaction vessels are sequentially connected; the reaction mixture successively moves to each of the reaction vessels; and the housing chamber includes a baffle (9) configured to narrow the cross-sectional area of the gas phase part at the boundary between at least one pair of adjacent reaction vessels or in the vicinity of the boundary.

A continuous production device and a continuous production method which are configured to produce a polymer and can efficiently advance solution polycondensation with a simple device configuration which is easy to wash and maintenance. A continuous production device (100) includes a reactor main body (1), divider plates (6a to 6c) configured to divide the interior of the reactor main body into a plurality of reaction vessels (2a to 2d), and a raw material supply unit. The divider plate has a rotation center. Gas-phase parts of the reaction vessels adjacent to each other are communicating with each other, and liquid-phase parts of the reaction vessels adjacent to each other are communicating with each other. A reaction mixture generated in the reaction vessel sequentially moves through the reaction vessels.

The present disclosure relates to oxazoline modified lubricant additives that have dispersant properties and lubricating oil compositions including such dispersant lubricant additives. The disclosure also relates to the use of lubricant compositions comprising the additives of the disclosure for improving the soot or sludge handling characteristics of an engine lubricant composition while providing robust and consistent frictional performance at the same time.

A diblock copolymer, polymer vesicle, and method of forming a polymer vesicle are provided. The diblock polymer includes a hydrophilic first block and a second block including amine containing monomers and hydrophobic monomers. The polymer vesicle includes a diblock copolymer with a hydrophilic first block and a second block including amine containing monomers and hydrophobic monomers, and at least one active agent loaded in the polymer vesicle. The second block forms an inner hydrophobic domain of a vesicle membrane and the hydrophilic block forms a corona facing the exterior and aqueous interior of the vesicle membrane, the corona providing an outer shell that stabilizes the vesicle in aqueous media. The method of forming the polymer vesicle includes synthesizing the diblock copolymer through a polymerization technique selected from the group consisting of addition polymerization, condensation polymerization, and a combination thereof, providing at least one active agent, and assembling the polymer vesicle, the diblock copolymer including a hydrophilic first block and a second block with amine containing monomers and hydrophobic monomers.

Two part curable compositions are provided, which include a cure accelerator defined with reference to compounds shown in structure I ##STR00001##
where A is CH.sub.2 or benzyl, R is C.sub.1-10 alkyl, R is H or C.sub.1-10 alkyl, or R and R taken together may form a four to seven membered ring fused to the benzene ring, R is optional, but when R is present, R is halogen, alkyl, alkenyl, cycloalkyl, hydroxyalkyl, hydroxyalkenyl, alkoxy, amino, alkylene- or alkenylene-ether, alkylene (meth)acrylate, carbonyl, carboxyl, nitroso, sulfonate, hydroxyl or haloalkyl, and EWG is as shown, an electron withdrawing group, such as nitro, nitrile, carboxylate or trihaloalkyl.

An aromatic polysulfone resin having a yellowness index of 50 or higher and a weight average molecular weight of 25,000 to 45,000 is provided.