摘要:
Suggested are paint and coating remover compositions, comprising (a) a first solvent selected from the group consisting of carboxylic acid dialkylamides, and (b) a second solvent selected from the group consisting of C 1 -C 6 alcohols, C 2 -C 10 polyols, C 2 -C 6 ketones, NMP, DMF, mono or dicarboxylic acid esters, aromatic hydrocarbons, terpenes, nitromethane and their mixtures.
摘要:
Suggested are degreasing compositions comprising at least one dialkyl amide according to general formula (I)
R 1 CO-NR 2 R 3 (I)
in which R 1 CO stands for a linear or branched, saturated or unsaturated, aliphatic or aromatic, optionally hydroxysubstituted acyl radical having 2 to 56 carbon atoms, and R 2 and R 3 represent independently from each other alkyl radicals having 1 to 6 carbon atoms.
摘要:
Suggested is a process for the production of modified alkyd resins by polymerisation of (a) Polyhydric alcohols, (b) Polycarboxylic acids, dicarboxylic acids or their anhydrides, and (c) Unsaturated oils or unsaturated fatty acids in the presence of organic solvents, which is characterised in that unsaturated dialkyl amides are used as solvents.
摘要:
Suggested are biocide compositions, comprising (a) 2-Furoic and/or Tetrahydro-2-furoic acid amides; (b) Biocides and optionally (c) Oil components or co-solvents and/or (d) Emulsifiers. The compositions show high solubility for biocides and improved emulsification properties.
摘要:
Suggested are bituminous compositions for road construction, comprising as binders (a) at least one thinner selected from the group consisting of dialkylamides derived from unsaturated fatty acids and being capable to be chemically converted on contact with air, after the binder has been spread, and (b) at least one catalyst for the polymerization of the thinner under the action of oxygen.
摘要:
Suggested is a continuous process for the production of mono- or dicarboxylic acid alkyl amides, which is characterised in that: (a) fresh mono- or dicarboxylic acid is placed into a first reactor (R1) connected with a distillation column (C1) and subjected to a reaction with ammonia or gaseous alkyl amine to form a pre-mixture consisting of mono- or dicarboxylic acid alkyl amide and unreacted mono- or dicarboxylic acid, while the water of condensation is distilled off; (b) said pre-mixture is transferred into a second reactor (R2) also equipped with a distillation column (C2) and subjected to a further reaction with ammonia or gaseous alkyl amine to substantially convert all unreacted mono- or dicarboxylic acid into mono- or dicarboxylic acid alkyl amide; and (c) all unreacted ammonia or gaseous alkyl amine is transferred into the first reactor (R1) to start the amidation reaction.