Plate evaporator

Claim 2

A plate evaporator of the rising and/or falling film type comprising a series of heat exchange plates disposed substantially vertically in spaced face-to-face relationship to define evaporation passages through which a medium to be evaporated is adapted to pass in a flow direction, said plates also defining heating medium passages alternating with said evaporation passages, at least one of two adjacent plates defining an evaporation passage being provided with bulges which, as compared with imaginary planar plates spaced the same distance apart as said two adjacent plates, entail a reduced volume of the evaporation passage, the volume of said bulges, as measured from a said imaginary planar plate in the plane of the bulged plate, decreasing per unit of length in said flow direction through the evaporation passage over a substantial length thereof, the cross-sectional area of each evaporation passage increasing in said flow direction over said substantial length of the evaporation passage, the wetted perimeter of each evaporation passage, as seen in cross-section, decreasing in said flow direction over said substantial length.

Claim 3

The evaporator of claim 1, in which said bulges have ridges.

Claim 4

The evaporator of claim 2, in which said ridges extend substantially vertically with decreasing height in said flow direction.

Claim 5

The evaporator of claim 3, in which the two plates defining an evaporation passage have oppositely directed ridges, the ridges on one plate being displaced half the pitch distance with respect to the ridges on the other plate.

Claim 6

The evaporator of claim 1, in which the main part of each evaporation passage is free from support points between the two plates defining the evaporation passage.

Claim 7

The evaporator of claim 2, in which the two plates defining an evaporation passage have oppositely directed ridges, the evaporator comprising also means forming support points between the two plates defining a said heating medium passage, said support points being located in the plate regions between said ridges.

Claim 8

The evaporator of claim 6, in which said two plates defining a heating medium passage are located with their respective ridges opposite each other.

Claim 9

The evaporator of claim 6, in which said means are spacer elements for keeping in spaced relation the two plates defining a said heating medium passage.

Claim 10

The evaporator of claim 8, in which said spacer elements are bars extending across a plurality of said ridges.

Claim 11

The evaporator of claim 11, in which the width of each said evaporation passage decresses in said flow direction, thereby further decreasing the wetted perimeter of the evaporation passage in said flow direction.

Claim 12

The evaporator of claim 1, in which the two plates of each said pair defining an evaporation passage diverge from each other in said flow direction, thereby further increasing the cross-sectional area of the evaporation passage in said flow direction.

Claim 13

A plate evaporator of the rising and/or falling film type comprising a series of heat exchange plates disposed substantially vertically in spaced face-to-face relationship to define evaporation passages through which a medium to be evaporated is adapted to pass in a flow direction, said plates also defining heating medium passages alternating with said evaporation passages, there being a series of adjacent bulges on at least one of two adjacent plates defining an evaporation passage, said bulges on said one plate protruding into said evaporation passage and acting to reduce the volume of said evaporation passage by the volume of said bulges as measured froman imaginary planar plate in the plane of said one plate, each bulge on said one plate forming an elongated protrusion extending substantially continuously in said flow direction over a substantial length of said evaporation passage and defining with each adjacent bulge on said one plate a valley extending substantially continuously in said flow direction, each said bulge decreasing in volume per unit of length in said flow direction over said substantial length so that the cross-sectional area of the adjacent evaporation passage increases in said flow direction over said substantial length, the wetted perimeter of each evaporation passage, as seen in cross-section, decreasing in said flow direction over said substantial length and being substantially smaller at the downstream end of said substantial length than at the upstream end thereof.

Claim 14

A plate evaporator of the rising and/or falling film type comprising a series of heat exchange plates disposed substantially vertically in spaced face-to-face relationship to define evaporation passages through which a medium to be evaporated is adapted to pass in a flow direction, said plates also defining heating medium passages alternating with said evaporation passages, there being a series of adjacent bulges on at least one of two adjacent plates defining an evaporation passage, said bulges on said one plate protruding into said evaporation passage and acting to reduce the volume of said evaporation passage by the volume of said bulges as measured froman imaginary planar plate in the plane of said one plate, each bulge on said one plate forming an elongated protrusion extending substantially continuously in said flow direction over a substantial length of said evaporation passage and defining with each adjacent bulge on said one plate a valley extending substantially continuously in said flow direction, each said bulge decreasing in volume per unit of length in said flow direction over said substantial length so that the cross-sectional area of the adjacent evaporation passage increases in said flow direction over said substantial length, the wetted perimeter of each evaporation passage, as seen in cross-section, decreasing in said flow direction over said substantial length and being substantially smaller at the downstream end of said substantial length than at the upstream end thereof.

Claim 15

The evaporator of claim 12, in which said bulges have ridges.

Claim 16

The evaporator of claim 13, in which the height of each ridge decreases in said flow direction.

Claim 17

The evaporator of claim 13, in which the two plates defining an evaporation passage have oppositely directed ridges, the ridges on one plate being displaced half the pitch distance relative to the ridges on the other plate.

Claim 18

A plate evaporator of the rising and/or falling film type comprising a series of heat exchange plates disposed substantially vertically in face-to-face relationship, there being a space between each pair of adjacent plates so as to provide a series of interplate spaces, spacer means located in alternate ones of said spaces, each spacer means forming with adjacent plates an evaporation passage through which a medium to be evaporated is adapted to pass in a flow direction, the others of said spaces forming heating medium passages alternating with said evaporation passages, there being a series of adjacent bulges on at least one of two adjacent plates defining an evaporation passage, said bulges on said one plate protruding into said evaporation passage and acting to reduce the volume of said evaporation passage by the volume of said bulges as measured from an imaginary planar plate in the plane of said one plate, each bulge on said one plate forming an elongated protrusion extending substantially continuously in said flow direction over a substantial length of said evaporation passage and defining with each adjacent bulge on said one plate a valley extending substantially continuously in said flow direction, each said bulge decreasing in volume per unit of length in said flow direction over said substantial length so that the cross-sectional area of the adjacent evaporation passage increases in said flow direction over said substantial length, each said spacer means having sides forming opposing sides of the corresponding evaporation passage and being so dimensioned that the spacing between the adjacent plates increases in said flow direction, thereby further increasing said cross-sectional area in said flow direction, the perimeter of each evaporation passage, as seen in cross-section, being defined by opposed surfaces of the adjacent plates and said opposing sides of the evaporation passage, those parts of said perimeter defined by said opposed surfaces of the adjacent plates decreasing in said flow direction over said substantial length.

Claim 19

A plate evaporator of the rising and/or falling film type comprising a series of heat exchange plates disposed substantially vertically in face-to-face relationship, there being a space between each pair of adjacent plates so as to provide a series of interplate spaces, spacer means located in alternate ones of said spaces, each spacer means forming with adjacent plates an evaporation passage through which a medium to be evaporated is adapted to pass in a flow direction, the others of said spaces forming heating medium passages alternating with said evaporation passages, there being a series of adjacent bulges on at least one of two adjacent plates defining an evaporation passage, said bulges on said one plate protruding into said evaporation passage and acting to reduce the volume of said evaporation passage by the volume of said bulges as measured from an imaginary planar plate in the plane of said one plate, each bulge on said one plate forming an elongated protrusion extending substantially continuously in said flow direction over a substantial length of said evaporation passage and defining with each adjacent bulge on said one plate a valley extending substantially continuously in said flow direction, each said bulge decreasing in volume per unit of length in said flow direction over said substantial length so that the cross-sectional area of the adjacent evaporation passage increases in said flow direction over said substantial length, each said spacer means having sides forming opposing sides of the corresponding evaporation passage and being so dimensioned that the spacing between the adjacent plates increases in said flow direction, thereby further increasing said cross-sectional area in said flow direction, the perimeter of each evaporation passage, as seen in cross-section, being defined by opposed surfaces of the adjacent plates and said opposing sides of the evaporation passage, those parts of said perimeter defined by said opposed surfaces of the adjacent plates decreasing in said flow direction over said substantial length.

Claim 20

The evaporator of claim 16, in which the width of each evaporation passage, as measured from one to the other of said opposing sides, decreases in said flow direction, thereby further decreasing said part of the perimeter in said flow direction.