Abstract:
PROBLEM TO BE SOLVED: To provide a new production method of monochloroethylene carbonate, which hardly causes the formation of undesired chlorinated decomposition products. SOLUTION: The production method of monochloroethylene carbonate comprises (a) reacting ethylene carbonate with a chlorine gas in a liquid phase under the irradiation of ultraviolet rays and (b) introducing a separate inert gas feed into the liquid phase. COPYRIGHT: (C)2009,JPO&INPIT
Abstract:
The invention is directed to an improved, reliably performable process for preparing triallyl isocyanurate (TAIC) by Cu 2+ -catalysed rearrangement of triallyl cyanurate (TAC) at at least 90°C. According to the invention, TAC and, if required, also a Cu 2+ catalyst and solvent are fed continuously to a start reaction mixture after onset of the initially inhibited isomerization reaction, the isomerization is performed at from 90 to 160°C and an amount of reaction mixture equivalent to the amount of reactant is drawn off continuously and sent to the workup. Preference is given to effecting the isomerization in TAIC as the reaction medium.
Abstract:
The invention is directed to an improved, reliably performable process fo r preparing triallyl isocyanurate (TAIC) by Cu2+-catalysed rearrangement of triallyl cyanurate (TAC) at at least 90øC. According to the invention, TAC a nd, if required, also a Cu2+ catalyst and solvent are fed continuously to a start reaction mixture after onset of the initially inhibited isomerization reaction, the isomerization is performed at from 90 to 160øC and an amount o f reaction mixture equivalent to the amount of reactant is drawn off continu ously and sent to the workup. Preference is given to effecting the isomeriza tion in TAIC as the reaction medium.
Abstract:
The invention relates to a process for preparing monochloroethylene carbonate comprising: (a) reacting ethylene carbonate with chlorine gas in the liquid phase under the irradiation of UV light and (b) introducing a separate feed of an inert gas into the liquid phase. A process further comprising the subsequent conversion of the monochloroethylene carbonate to vinylene carbonate is also claimed.
Abstract:
La invención está dirigida a un proceso mejorado, relializable eficazmente para preparar isocianurato de trialilo (TAIC) mediante la transposición catalizada por Cu2+- de cianurato de trialilo (TAC) a por lo menos 90ºC. De conformidad con la invención, TAC y si se requiere, también un catalizador de Cu2+ y solvente son alimentados continuamente a una mezcla de reacción de partida después del inicio de la reacción de isomerización inhibida inicialmente, la isomerización es realizada a desde 90 hasta 160ºC y una cantidad de mezcla de reacción equivalente a la cantidad de reactivo es retirada continuamente y enviada al tratamiento final. Se da preferencia a llevar a cabo la isomerización en TAIC como la reacción media.
Abstract:
The invention is directed to an improved, reliably performable process for preparing triallyl isocyanurate (TAIC) by Cu2+-catalysed rearrangement of triallyl cyanurate (TAC) at at least 90°C. According to the invention, TAC and, if required, also a Cu2+ catalyst and solvent are fed continuously to a start reaction mixture after onset of the initially inhibited isomerization reaction, the isomerization is performed at from 90 to 160°C and an amount of reaction mixture equivalent to the amount of reactant is drawn off continuously and sent to the workup. Preference is given to effecting the isomerization in TAIC as the reaction medium.
Abstract:
Preparation of triallylisocyanurate comprises rearranging triallylcyanurate in the presence of copper (II) salts (0.01-1 wt.%) at at least 90[deg]C, preferably 90-160[deg]C; introducing separately or in a mixture of triallylcyanurate and copper (II) salts into the triallylisocyanurate; cooling the reaction mixture at less than 90[deg]C; continuously adding the reaction mixture and isolating the triallylisocyanurate from the reaction mixture.
Abstract:
Preparation of triallylisocyanurate comprises rearranging triallylcyanurate in the presence of copper (II) salts (0.01-1 wt.%) at at least 90[deg]C, preferably 90-160[deg]C; introducing separately or in a mixture of triallylcyanurate and copper (II) salts into the triallylisocyanurate; cooling the reaction mixture at less than 90[deg]C; continuously adding the reaction mixture and isolating the triallylisocyanurate from the reaction mixture.