Apparatus and method for removing halogens generated during preparation of polybutene
Disclosed are an apparatus and a method for removing halogens generated during the preparation of polybutene, which are capable of improving the utilization of polybutene and light polymers by removing halogen components contained in the polybutene and the light polymers. The method for removing halogens generated during the preparation of polybutene comprises the steps of: preparing a reaction product by supplying a catalyst and a reaction raw material to a reactor and polymerizing; removing a catalyst component from the reaction product and neutralizing; separating the reaction product into an organic compound and impurities comprising the catalyst component; heating the organic compound to distill an unreacted material; and removing a halogen component in a remaining polymerization mixture after the distillation using a halogen removing catalyst, or removing a halogen component in polybutene and light polymers obtained from the polymerization mixture using the halogen removing catalyst.
1. A method for removing halogens generated during preparation of polybutene, the method comprising:
preparing a reaction product by supplying a catalyst and a reaction raw material to a reactor and polymerizing;
washing a catalyst component from the reaction product and neutralizing;
separating the reaction product into an organic compound and impurities comprising the catalyst component;
heating the organic compound to distill an unreacted material; and
removing a halogen component in a remaining polymerization mixture after the distillation using a halogen removing catalyst, or removing a halogen component in polybutene and light polymers obtained from the polymerization mixture using the halogen removing catalyst,
wherein the halogen removing catalyst is iron halide selected from the group consisting of ferrous chloride (FeCl 2 ), ferric chloride (FeCl 3 ), ferrous fluoride (FeF 2 ) and ferric fluoride (FeF 3 ).
2. The method for removing halogens generated during preparation of polybutene according to claim 1 , wherein a halogen content of the polymerization mixture or the light polymers after reaction with the halogen removing catalyst at 50 to 250° C. is less than 50 ppm.
3. The method for removing halogens generated during preparation of polybutene according to claim 1 , wherein the form of the halogen removing catalyst is selected from the group consisting of a powder type, a spherical type, a cylindrical type and a tablet type, and the halogen removing catalyst is processed using an inorganic binder and an organic binder such that the diameter of the halogen removing catalyst is 0.1 to 100 mm.
4. The method for removing halogens generated during preparation of polybutene according to claim 1 , wherein the halogen removing catalyst is obtained by dissolving iron halide in water and impregnating in aluminum oxide (Al 2 O 3 ), zeolite, or clay, or by mixing the iron halide with aluminum oxide (Al 2 O 3 ), zeolite, or clay.
5. The method for removing halogens generated during preparation of polybutene according to claim 1 , further comprising removing halogen acid generated after removing the halogen component using a halogen acid adsorbent.
6. The method for removing halogens generated during preparation of polybutene according to claim 5 , wherein the halogen acid adsorbent is 0.1 to 100 mm in the particle diameter, and the halogen acid adsorbent is selected from the group consisting of calcium hydroxide (Ca(OH) 2 ), calcium oxide (CaO), calcium carbonate (CaCO 3 ), calcium chloride (CaCl 2 ), potassium hydroxide (KOH), potassium carbonate (K 2 CO 3 ), potassium bicarbonate (KHCO 3 ), potassium chloride (KCl), sodium hydroxide (NaOH), sodium carbonate (Na 2 CO 3 ), sodium bicarbonate (NaHCO 3 ), solid silica, solid alumina, a strongly basic anion exchange resin and a strongly acidic cation exchange resin.
7. An apparatus for removing halogens generated during preparation of polybutene, the apparatus comprising:
a reactor, into which a catalyst and a reaction raw material are supplied and polymerized to produce a reaction product;
a neutralizing/washing bath for washing the catalyst from the reaction product and neutralizing the reaction product;
a separating bath for separating the reaction product into an organic compound and impurities comprising the catalyst component;
a C4 distillation column for distilling an unreacted material among the organic compound; and
a halogen removing column for removing a halogen component in a remaining polymerization mixture after the distillation using the halogen removing catalyst, or removing a halogen component in polybutene and light polymers obtained from the polymerization mixture using the halogen removing catalyst;
wherein the halogen removing catalyst is iron halide selected from the group consisting of ferrous chloride (FeCl 2 ), ferric chloride (FeCl 3 ), ferrous fluoride (FeF 2 ) and ferric fluoride (FeF 3 ).