Apparatus for continuously producing polyisocyanate
An apparatus for continuously producing polyisocyanate is provided for quickly contacting polyamine and carbonyl chloride in order to suppress an undesirable reaction between polyamine and polyisocyanate so that a by-product can be reduced and the yield of polyisocyanate can be improved. In a circulatory line 7 , a material-mixing portion 8 , a high-shear pump 3 , a reactor 4 , a liquid-feeding pump 5 and a cooler 6 are interposed in series along the direction of the flow of a reaction solution, thereby forming a closed line. In this apparatus 1 , after polyamine and carbonyl chloride are supplied in the material-mixing portion 8 , the reaction solution is sheared by the high-shear pump 3 in a state where the contact of the polyamine with the reaction solution is minimized. Thus, the formation of a urea compound as a by-product can be suppressed and the yield of polyisocyanate can be improved.
1. An apparatus for continuously producing polyisocyanate by reacting polyamine with carbonyl chloride, comprising:
a reactor and a circulatory unit for circulating a reaction solution to the reactor,
the circulatory unit comprising:
1) a circulatory line for circulating the reaction solution,
2) polyamine supplying unit for supplying polyamine to the circulatory line,
3) carbonyl chloride supplying unit for supplying carbonyl chloride to the circulatory line,
4) polyamine-carbonyl chloride contacting unit for contacting the polyamine supplied from the polyamine supplying unit to the circulatory line and the carbonyl chloride supplied from the carbonyl chloride supplying unit to the circulatory line in the presence of the circulating reaction solution, and
5) mixing unit for mixing the carbonyl chloride and the polyamine contacted by the contacting unit, and the circulated reaction solution by shearing, wherein the polyamine supplied from the polyamine supplying unit, the carbonyl chloride supplied from the carbonyl supplying unit, and the reaction solution substantially form three layers from the contacting unit to the mixing unit.
2. The apparatus for continuously producing polyisocyanate according to claim 1 , wherein the polyamine supplied from the polyamine supplying unit to the circulatory line and the polyisocyanate in the circulated reaction solution are not substantially reacted in the circulatory unit.
3. The apparatus for continuously producing polyisocyanate according to claim 1 , wherein a distance between the contacting unit and the mixing unit is 1,000 mm or less.
4. The apparatus for continuously producing polyisocyanate according to claim 1 , wherein a linear velocity of the polyamine supplied from the polyamine supplying unit to the circulatory line is from 0.5 to 10 m/sec in a cross section of the polyamine supplying unit,
a linear velocity of the carbonyl chloride supplied from the carbonyl chloride supplying unit to the circulatory line is from 0.5 to 10 m/sec in a cross section of the carbonyl chloride supplying unit, and
a linear velocity of the reaction solution within the circulatory line immediately before supplying to the contacting unit is from 0.3 to 5 m/sec.
5. The apparatus for continuously producing polyisocyanate according to claim 1 , wherein a cooling device is interposed in a middle of the circulatory line, and
a temperature of the reaction solution after supplying the polyamine and the carbonyl chloride within the circulatory line is controlled to 120° C. or lower.
6. An apparatus for continuously producing polyisocyanate by reacting polyamine with carbonyl chloride, comprising:
a reactor and a circulatory unit for circulating a reaction solution to the reactor,
the circulatory unit comprising:
1) a circulatory line for circulating the reaction solution,
2) polyamine supplying unit for supplying polyamine to the circulatory line,
3) carbonyl chloride supplying unit for supplying carbonyl chloride to the circulatory line,
4) polyamine-carbonyl chloride contacting unit for contacting the polyamine supplied from the polyamine supplying unit to the circulatory line and the carbonyl chloride supplied from the carbonyl chloride supplying unit to the circulatory line in the presence of the circulating reaction solution, and
5) mixing unit for mixing the carbonyl chloride and the polyamine contacted by the contacting unit, and the circulated reaction solution by shearing, wherein the polyamine supplying unit comprises a polyamine supplying line having an flow-out side end portion that is inserted into the circulatory line,
the carbonyl chloride supplying unit comprises a carbonyl chloride supplying line having a flow-out side end portion that is inserted into the circulatory line,
the flow-out side end portion of the polyamine supplying line is provided adjacent to an inner wall surface of the circulatory line, and opens toward the downstream side with respect to the flow of the reaction solution from the contacting unit to the mixing unit, and
the flow-out side end portion of the carbonyl chloride supplying line opens toward a flow-out solution of the polyamine supplied from the flow-out side end portion of the polyamine supplying line.
7. The apparatus for continuously producing polyisocyanate according to claim 6 , wherein the polyamine supplied from the polyamine supplying unit to the circulatory line and the polyisocyanate in the circulated reaction solution are not substantially reacted in the circulatory unit.
8. The apparatus for continuously producing polyisocyanate according to claim 6 , wherein a distance between the contacting unit-and the mixing unit is 1,000 mm or less.
9. The apparatus for continuously producing polyisocyanate according to claim 6 , wherein a linear velocity of the polyamine supplied from the polyamine supplying unit to the circulatory line is from 0.5 to 10 m/sec in a cross section of the polyamine supplying unit,
a linear velocity of the carbonyl chloride supplied from the carbonyl chloride supplying unit to the circulatory line is from 0.5 to 10 m/sec in a cross section of the carbonyl chloride supplying unit, and
a linear velocity of the reaction solution within the circulatory line immediately before supplying to the contacting unit is from 0.3 to 5 m/sec.
10. The apparatus for continuously producing polyisocyanate according to claim 6 , wherein a cooling device is interposed in a middle of the circulatory line, and
a temperature of the reaction solution after supplying the polyamine and the carbonyl chloride within the circulatory line is controlled to 120° C. or lower.