Modular plate and shell heat exchanger
US-9285172-B2 · Mar 15, 2016 · US
US10634433B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10634433-B2 |
| Application number | US-201616064581-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 5, 2016 |
| Priority date | Dec 22, 2015 |
| Publication date | Apr 28, 2020 |
| Grant date | Apr 28, 2020 |
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A distillation plant comprises an elongated vessel extending along a longitudinal axis and defining an inner space, and a plurality of plate heat exchangers, which in an operating position are arranged after each other along the longitudinal axis in the vessel. Each plate heat exchanger comprises a plurality of heat exchanger plates, each defining an extension plane. The heat exchanger plates form first plate interspaces and second plate interspaces. The first and second plate interspaces are arranged in an alternating order in the plate heat exchanger. At least one of the plate heat exchangers is associated with a respective opening through the vessel, and is removable from the operating position out of the vessel through the associated opening by being moved in a displacement direction, which is perpendicular to the extension plane of the heat exchanger plates.
Opening claim text (preview).
The invention claimed is: 1. A distillation plant comprising an elongated vessel extending along a longitudinal axis and defining an inner space, and a plurality of plate heat exchangers, which in an operating position are arranged after each other along the longitudinal axis of the vessel, wherein each plate heat exchanger comprises a first end plate, a second end plate and a plurality of heat exchanger plates, each of said heat exchanger plates defining an extension plane, wherein the heat exchanger plates are arranged between the first end plate and the second end plate to form first plate interspaces and second plate interspaces, the first and second plate interspaces being arranged in an alternating order in the plate heat exchanger, and wherein the first end plate and the heat exchanger plates of the plate heat exchangers are in the operating position provided in the inner space, a plurality of the plate heat exchangers are each associated with a respective opening through the vessel, and each of the plurality of plate heat exchangers is removable from the operating position out of the vessel through the associated opening by being moved in a displacement direction, which is perpendicular to the extension plane of the heat exchanger plates. 2. The distillation plant according to claim 1 , wherein the at least one of the plate heat exchangers is supported by a guide member, which permits the plate heat exchanger to be moved in the displacement direction. 3. The distillation plant according to claim 2 , wherein the guide member comprises a suspension rail in which the plate heat exchanger is movably suspended. 4. The distillation plant according to claim 2 , wherein the guide member comprises two guide rails on which the plate heat exchanger is movably provided. 5. The distillation plant according to claim 2 , wherein the second end plate of the at least one of the plate heat exchangers forms a cover sealingly closing the associated opening through the vessel. 6. The distillation plant according to claim 1 , wherein the plurality of plate heat exchangers comprises at least one primary plate heat exchanger in which the first plate interspaces are configured for condensation and the second plate interspaces are configured for evaporation, and wherein the at least one primary plate heat exchanger has a steam inlet, which extends perpendicularly to the extension plane of the heat exchanger plates and communicates with the first plate interspaces, and a steam outlet, which extends perpendicularly to the extension plane of the heat exchanger plates and communicates with the second plate interspaces. 7. The distillation plant according to claim 6 , comprising a sealing arrangement separating the steam inlet from the steam outlet of the at least one primary plate heat exchanger in the operating position in the inner space. 8. The distillation plant according to claim 7 , wherein the at least one primary plate heat exchanger comprises a first transition area extending perpendicularly to the extension plane of the heat exchanger plates between the steam inlet and the steam outlet, and a second transition area extending perpendicularly to the extension plane of the heat exchanger plates between the steam inlet and the steam outlet, and wherein the sealing arrangement comprises a first sealing member engaging the first transition area and a second sealing member engaging the second transition area. 9. The distillation plant according to claim 8 , wherein each of the first and second sealing members is inflatable from a rest position at a distance from the first transition area and the second transition area, respectively, to a sealing position at which each of the first and second sealing members engages the first transition area and the second transition area, respectively. 10. The distillation plant according to claim 8 , wherein the at least one primary plate heat exchanger comprises a respective gasket in each of the first plate interspaces and the second plate interspaces, and wherein each gasket extends to the first transition area and to the second transition area. 11. The distillation plant according to claim 6 , wherein the at least one primary plate heat exchanger has a liquid inlet port channel communicating with the second plate interspaces and connected to a liquid feed conduit for the supply of a liquid to be evaporated in the second plate interspaces, and a liquid outlet port channel communicating with the first plate interspaces and connected to a condensate discharge conduit for the discharge of a condensate from the first plate interspaces. 12. The distillation plant according to claim 11 , wherein the liquid inlet port channel and the liquid outlet port channel extend through the second end plate. 13. The distillation plant according to claim 11 , wherein the liquid inlet port channel and the liquid outlet port channel both extend through the first end plate. 14. The distillation plant according to claim 6 , comprising a plurality of effects, each effect comprising at least one primary plate heat exchanger, and wherein each effect comprises a liquid separator provided in the inner space downstream of the second plate interspaces. 15. The distillation plant according to claim 14 , wherein the inner space defines a plurality of subspaces, one for each effect, wherein each subspace defines a first part space communicating with the first plate interspaces and a second part space communicating with the second plate interspaces, and wherein a second part space of one effect communicates with a first part space of a subsequent effect. 16. The distillation plant according to claim 1 , wherein the extension plane of the heat exchanger plates of at least one of the plurality of plate heat exchangers extends in parallel with the longitudinal axis of the vessel. 17. A distillation plant comprising an elongated vessel extending along a longitudinal axis and defining an inner space, and a plurality of plate heat exchangers, which in an operating position are arranged after each other along the longitudinal axis of the vessel, wherein each plate heat exchanger comprises a first end plate, a second end plate and a plurality of heat exchanger plates, each heat exchanger plate defining an extension plane, and tie bolts extending through the first end plate and the second end plate of each plate heat exchanger for tightening the heat exchanger plates against each other, wherein the heat exchanger plates of each plate heat exchanger are arranged between the first end plate and the second end plate of the respective plate heat exchanger to form first plate interspaces and second plate interspaces, the first and second plate interspaces of each plate heat exchanger being arranged in an alternating order in the plate heat exchanger, the first end plate and the heat exchanger plates of each respective plate heat exchanger being positioned in the inner space when in the operating position, a plurality of openings passing through a wall of the vessel, each of the plurality of plate heat exchangers being associated with a respective one of the openings passing through the wall of the vessel, and each of the plurality of plate heat exchangers being removable from the operating position out of the vessel through the associated opening by being moved in a displacement direction that is perpendicular to the extension plane of the heat exchanger plates. 18. The distillation plant according to claim 17 , wherein each of the plate heat exchangers is supported on a re
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