Heat-exchanger reactor having mixing zones
The present invention relates to a heat-exchanger reactor comprising a vessel, at least one dividing member selected from plates, walls, or spiral sheets, which dividing member separates heat exchanging fluids into at least one heat exchanging zone from fluids into at least one mixing zone, and at least one flow-directing device having one or more ports or one or more injection ports, which flow-directing device is inserted into the mixing zone. The present invention relates also to uses of the heat-exchanger reactor.
1. A heat-exchanger reactor comprising: a vessel; one or more heat exchanger zones; one or more mixing zones; and at least one dividing member selected from plates, walls, or spiral sheets; which dividing member separates the heat exchanger zones from the mixing zones, and wherein the heat is transferred by conductivity in the dividing member between the mixing zones and the heat exchanger zones; the heat-exchanger reactor further comprises one or more flow-directing devices; wherein the flow-directing devices are at least one of, one or more tubes, one or more pipes, one or more conduits, one or more chambers, and one or more fluid sheet chambers, said flow-directing devices have at least one of one or more fluid ports and one or more injection ports for fluids, and the flow-directing devices being inserted into the one or more mixing zones, wherein the flow-directing device includes one or more tubes having ports for fluids, said tubes being mounted on a spiral inlet tube.
2. The heat-exchanger reactor according to claim 1 , wherein the one or more mixing zones comprises one or more static mixers.
3. The heat-exchanger reactor according to claim 1 , wherein the flow-directing device includes one or more tubes having ports for fluids, said tubes being mounted on a spiral inlet tube, combined with one or more fluid sheet chambers having perforations for fluids.
4. The chemical reactor according to claim 3 , wherein the pipes or the tubes have distance elements.
5. The chemical reactor according claim 3 , wherein the ports are nozzles or jet nozzles.
6. The heat-exchanger reactor according to claim 1 , wherein one or more ports are selected from the group consisting of one or more nozzles, one or more jet nozzles, one or more sprayers, one or more sprinklers, one or more ports having perforations for fluids, one or more ports having a fine distribution system with at least one of defined holes and defined slots.
7. The heat-exchanger reactor according to claim 1 , wherein the heat-exchanging zone is a spiral heat exchanger.
8. The heat-exchanger reactor according to claim 1 , wherein the heat-exchanging zone is a plate heat exchanger.
9. The heat-exchanger reactor according to claim 1 , wherein the pipes or the tubes have distance elements.
10. The heat-exchanger reactor according to claim 1 , wherein the ports are nozzles or jet nozzles.
11. The heat-exchanger reactor according claim 1 , wherein all the ports or the injection ports are substantially identical, or to all the ports or injection ports are different ports selected from the group consisting of nozzles, jet nozzles, injection ports, sprinklers, sprayers.
12. The heat-exchanger reactor according to claim 1 , wherein the ports or the injection ports are spaced apart with substantially identical spacing therebetween, or different spacing on the inlet pipes.
13. A chemical reactor comprising a vessel, one or more heat exchanger zones, one or more mixing zones, and at least one dividing member selected from plates, walls, or spiral sheets, which dividing member separates the heat exchanger zones from the mixing zones, and wherein the heat is transferred by conductivity in the dividing member between the mixing zones and the heat exchanger zones, the chemical reactor comprises further one or more flow-directing devices, wherein the flow-directing devices being one or more tubes, one or more pipes, one or more conduits, or combinations of these, said flow-directing devices have one or more ports fluids or one or more injection ports for fluids or combinations thereof, and the flow-directing devices being inserted into the one or more mixing zones, and wherein said tubes or said pipes or said conduits being mounted on a spiral inlet tube.
14. The chemical reactor according to claim 13 , wherein the heat-exchanging zone is a spiral heat exchanger.
15. The chemical reactor according to claim 13 , wherein the pipes or the tubes have distance elements.
16. The chemical reactor according to claim 13 , wherein the ports are nozzles or jet nozzles.
17. A chemical reactor comprising a vessel, a heat exchanger zone, one or more mixing zones, and one or more flow-directing devices, said heat-exchanging zone being a spiral heat exchanger, said flow-directing devices being one or more tubes, one or more pipes, one or more conduits, or combinations of these, said flow-directing devices have one or more ports fluids or one or more injection ports for fluids or combinations of these, and the flow-directing devices being inserted into the one or more mixing zones in the spiral heat exchanger, and wherein said tubes or said pipes or said conduits being mounted on a spiral inlet tube.