Method of preparing dichloropropanol using glycerol with improved selectivity for dichloropropanol
A method of preparing dichloropropanol using glycerol. The method includes: chlorination of glycerol including a plurality of chlorination reaction stages using a catalyst; and a water-removing stage performed between the reaction stages, independently of the reaction stages.
1. A method of preparing dichloropropanol, the method comprising:
performing a plurality of chlorination reaction stages of glycerol using a catalyst,
wherein the plurality of chlorination reaction stages produce water as a by-product and the catalyst is acetic acid,
wherein, in each of the chlorination reaction stages, a reaction product of the catalyst with glycerol is produced as a by-product, which functions as a catalyst for the chlorination of glycerol, and
wherein a boiling point of the reaction product of the catalyst with glycerol is higher than that of water; and
performing a water-removing stage between the chlorination reaction stages, independently of the chlorination reaction stages,
wherein the chlorination reaction stages comprise converting glycerol into monochloropropanediol (MCP) and converting monochloropropanediol (MCP) into dichloropropanol (DCP),
wherein the water-removing stage is performed using the boiling point difference between water and materials other than water,
wherein a chlorinating agent is added to a chlorination reaction stage prior to the water-removing stage, and a separate chlorinating agent other than a chlorinating agent originated from the chlorination reaction stage prior to the water-removing stage is not added to the water-removing stage,
wherein a separate catalyst other than a catalyst originated from the chlorination reaction stage prior to the water-removing stage is not added to a chlorination reaction stage after the water-removing stage.
2. The method of claim 1 , wherein the reaction product of the catalyst with glycerol comprises a glycerol ester of acetic acid.
3. The method of claim 1 , wherein the water-removing stage is performed when a glycerol-conversion rate is in a range of about 90 to about 100%, a monochloropropanediol-conversion rate is in a range of about 20 to about 60%.
4. The method of claim 1 , wherein the chlorination agent comprises hydrogen chloride gas or hydrochloric acid.
5. The method of claim 1 , wherein the chlorination reaction stages are performed in at least one reactor selected from a group consisting of a batch reactor, a semi-batch reactor, a continuous stirred tank reactor (CSTR), and a plug flow reactor.
6. A method of preparing epichlorohydrin (ECH) using dichloropropanol prepared by chlorination of glycerol, the method comprising a method of preparing dichloropropanol according to claim 1 .