The present invention relates to a production method of hexachloroacetone, including performing a reaction between at least one kind of compound (A) selected from the group consisting of acetone and chloroacetones having a chlorine atom number of from 1 to 5, and a chlorine molecule (B) in a solvent in the presence of an activated carbon, to obtain the hexachloroacetone.

The present invention relates to a production method of hexachloroacetone, including performing a reaction between at least one kind of compound (A) selected from the group consisting of acetone and chloroacetones having a chlorine atom number of from 1 to 5, and a chlorine molecule (B) in a solvent in the presence of an activated carbon, to obtain the hexachloroacetone.

The present invention relates to a production method of hexachloroacetone, including performing a reaction between at least one kind of compound (A) selected from the group consisting of acetone and chloroacetones having a chlorine atom number of from 1 to 5, and a chlorine molecule (B) in a solvent in the presence of an activated carbon, to obtain the hexachloroacetone.

A process for the preparation of a compound of formula (I) wherein R.sub.1 is hydrogen, fluoro or chloro; which process comprises: a) reacting a compound of formula (II) wherein R.sub.1 is hydrogen, fluoro or chloro; with a nitration agent to the compound of formula (III) wherein R.sub.1 is hydrogen, fluoro or chloro; b) reacting the compound of formula (III) with trichloroisocyanuric acid in the presence of sulfuric acid or fuming sulfuric acid to the compound of formula (IV) wherein R1 is hydrogen, fluoro or chloro; and c) reacting the compound of formula (III) with chlorine gas at a temperature from 180° C. to 250° C. to the compound of formula (I).

##STR00001##

A process for the preparation of a compound of formula (I) wherein R.sub.1 is hydrogen, fluoro or chloro; which process comprises: a) reacting a compound of formula (II) wherein R.sub.1 is hydrogen, fluoro or chloro; with a nitration agent to the compound of formula (III) wherein R.sub.1 is hydrogen, fluoro or chloro; b) reacting the compound of formula (III) with trichloroisocyanuric acid in the presence of sulfuric acid or fuming sulfuric acid to the compound of formula (IV) wherein R1 is hydrogen, fluoro or chloro; and c) reacting the compound of formula (III) with chlorine gas at a temperature from 180° C. to 250° C. to the compound of formula (I).

##STR00001##

A process for the preparation of a compound of formula (I) wherein R.sub.1 is hydrogen, fluoro or chloro; which process comprises: a) reacting a compound of formula (II) wherein R.sub.1 is hydrogen, fluoro or chloro; with a nitration agent to the compound of formula (III) wherein R.sub.1 is hydrogen, fluoro or chloro; b) reacting the compound of formula (III) with trichloroisocyanuric acid in the presence of sulfuric acid or fuming sulfuric acid to the compound of formula (IV) wherein R1 is hydrogen, fluoro or chloro; and c) reacting the compound of formula (III) with chlorine gas at a temperature from 180° C. to 250° C. to the compound of formula (I).

##STR00001##

The invention relates to a process for the preparation of a compound of formula I (I), wherein R.sub.1 is hydrogen, fluoro or chloro; which process comprises a) reacting a compound of formula II (II), wherein R.sub.1 is hydrogen, fluoro or chloro; with a nitration agent to the compound of formula (III), wherein R.sub.1 is hydrogen, fluoro or chloro; and b) reacting the compound of formula III with chlorine gas at temperature from 180° C. to 250° C. to the compound of formula I.

##STR00001##

The invention relates to a process for the preparation of a compound of formula I (I), wherein R.sub.1 is hydrogen, fluoro or chloro; which process comprises a) reacting a compound of formula II (II), wherein R.sub.1 is hydrogen, fluoro or chloro; with a nitration agent to the compound of formula (III), wherein R.sub.1 is hydrogen, fluoro or chloro; and b) reacting the compound of formula III with chlorine gas at temperature from 180° C. to 250° C. to the compound of formula I.

##STR00001##

Provided are a complex prepared from ammonium salt-containing ligands and having such an equilibrium structural formula that the metal center takes a negative charge of 2 or higher, and a method for preparing polycarbonate via copolymerization of an epoxide compound and carbon dioxide using the complex as a catalyst. When the complex is used as a catalyst for copolymerizing an epoxide compound and carbon dioxide, it shows high activity and high selectivity and provides high-molecular weight polycarbonate, and thus easily applicable to commercial processes. In addition, after forming polycarbonate via carbon dioxide/epoxide copolymerization using the complex as a catalyst, the catalyst may be separately recovered from the copolymer.

Provided are a complex prepared from ammonium salt-containing ligands and having such an equilibrium structural formula that the metal center takes a negative charge of 2 or higher, and a method for preparing polycarbonate via copolymerization of an epoxide compound and carbon dioxide using the complex as a catalyst. When the complex is used as a catalyst for copolymerizing an epoxide compound and carbon dioxide, it shows high activity and high selectivity and provides high-molecular weight polycarbonate, and thus easily applicable to commercial processes. In addition, after forming polycarbonate via carbon dioxide/epoxide copolymerization using the complex as a catalyst, the catalyst may be separately recovered from the copolymer.