HEAT EXCHANGER OF FALLING FILM TYPE

Abstract: In a heat exchanger of falling film type comprising heat exchange plates with area enlarging corrugation forming ridges and valleys extending in the falling film direction, repeated redistribution of the falling film is brought about by having the ridges and the valleys extending continuously within each of a number of zones formed one after the other in the falling direction, whereas the ridges and the valleys with regard to two consecutive zones are laterally displaced in relation to each other such that the ridges and the valleys, respectively, in one zone extend in alignment with the valleys and the ridges, respectively, in a consecutive zone.

Description: Heat exchanger of falling film type This invention relates to a heat exchanger of falling film type comprising heat exchange plates with area enlarging corrugation forming ridges and valleys extending in the falling film direction. When designing heat exchange surfaces for falling film appara¬ tuses like falling film coolers and falling film evaporators, for obtaining highest possible heat transfer between the falling film and the medium that is heat exchanged with the falling film, it is important to bring about a complete film cover of the falling film surfaces along the whole falling distance at the same time as the film shall be as thin as possible. Besides the problem to satisfy these two contradictory wishes, also other unfavourable, constructive considerations regarding the practical design of a plate heat exchanger have to be made for maintaining an even and unbroken falling film. Thus, interrup¬ tions and due to that unevennesses in the heat transfer surface have often to be made for instance for forming supporting points between two adjacent plate elements. Such supporting points in most heat exchanger cases can be positively utilized for turbu¬ lence generation but in the falling film case they constitute an obstacle for the formation of an unbroken film along the heat transfer surface. Prior falling film technics shows also examp¬ les of so serious disturbance of the falling film owing to bar elements arranged between the falling film surfaces that the bar elements at the same time have to be designed like and serve as a redistributor of the liquid film. The repeated slow down and acceleration of the falling liquid connected therewith lead to deteriorated heat transfer coefficients along a great part of the total falling distance. Furthermore, a folded or corrugated surface structure of the heat exchange elements are often wished in order to bring about area enlargement, increased strength and contact points between adjacent heat exchange elements. Such an area enlarging corruga¬ tion of the plate elements in. a falling film heat exchanger with ridges and valleys in the falling film direction, however, results in a further problem since the liquid of the formed fal¬ ling film tends to be accumulated in the valleys of the corruga¬ tion and cause film disruption at the ridges of the corrugation, the heat surface effectively utilized diminishing strongly. The obvious counter-measure to that is to increse the liquid load until the film does not burst any longer, which, however, results in an essentiall:, lower coefficient of thermal conduc¬ tance and, in the case of falling film evaporators, in a lower evaporation ratio than what would be possible otherwise. A purpose with the present invention is to bring about an embo¬ diment of heat exchange plates of a plate heat exchanger of the falling film type, in which the mentioned area enlarging corru¬ gation of the plate elements are utilized at. the same time as the mentioned problem with liquid accumulation in the valleys of the corrugation is eliminated. A further purpose with the invention is to bring about a plate heat exchanger of falling film type in which the mentioned area enlarging corrugation of the plate elements are utilized and the problem with liquid accumulation in the valleys of the corruga¬ tion is eliminated at the same time as the need of supporting points in the falling film passages is eliminated. A special purpose with the invention is to bring about a falling film evaporator of plate type in which the mentioned area enlar¬ ging corrugation of the plate elements is utilized and the prob¬ lem with liquid accumulation in the valleys of the corrugation is eliminated at the same time as the corrugation pattern of the plates is utilized in order to bring about evaporation passages with widening cross-section and diminishing heat transfer sur- face in the falling film direction. These purposes, according to the invention, are attained in a heat exchanger of the kind mentioned by way of introduction, which is principally characterized in that the ridges and the valleys formed by the corrugation of the heat exchanger plates extend continuously within each of a number of zones formed one after the other in the falling direction, that the ridges and the valleys of two consecutive zones are laterally displaced in relation to each other so that the ridges and the valleys, res¬ pectively, in one zone extend in alignment with the valleys and the ridges, respectively, in a consecutive zone, and that the corrugation of the plates in the transition passage between two consecutive zones forms connection surfaces for continuous liquid film flow from the lower end of the ridges and the valleys, respectively, in one zone to the upper end of the valleys and the ridges, respectively, in the consecutive zone. According to the invention the problem with the accumulation of the falling film liquid in the valleys of the plate corrugation is solved by a distribution, recurring several times along the plate, of the falling film from ridge to valley and from valley to ridge, respectively. At the same time the invention gives a unique possibility to bring about a repeated redistribution of the liquid of a falling film along a long falling distance with¬ out the falling liquid having to be slowed down as is the case in known falling film apparatuses, in which even distribution along a long falling distance is brought about by accumulating the liquid after certain intervals and by distributing the liquid again along the falling film surface by slit means. The last-mentioned way to redistribute the falling film, as has been mentioned above, is impaired by the drawback that the falling velocity reduced by the re-starts gives lower heat transfer coefficients along the distances where the falling film has to be accelerated up, during laminar flow, to velocities within the turbulent field which gives higher heat transfer coeffi¬ cients. The solution according to the invention is particularly advantageous since the redistribution mechanics does not require particular means and expensive mounting of the distribution means but can be wholly incorporated in the plate pattern by for instance conventional pressing of the plates. The different zones in the falling directions between which redistribution between ridge and valley occurs have for simpli¬ city reasons suitably uniform corrugation within each zone over the whole plate width, even if change between ridge and valley, of course, can occur on different height levels along different portions of the plate width. In the transition passages between two zones the corrugation pattern of the plates form a number of transfer surfaces which alternating in the cross-direction of the plate slope towards the falling line in one direction in order to connect a ridge with a valley and in opposite direction with the falling line in order to connect a valley with a ridge. The invention makes a good film cover possible over a falling film plate with corrugation ridges and valleys in the falling direction in plate lengths of several meters. The length of each zone with continuous ridges and valleys varies with selected corrugation pattern. As an example can be mentioned that, during practical experiments, with a wave length or graduation of the corrugation across the plate of 25-50 mm and a corrugation height between ridge top and valley bottom of 10-15 mm about three zones/meter have appeared to give excellent liquid distri- bution for a thin, continuous film. This can also be expressed so that the distribution problem has been eliminated according to the invention for long heat transfer plates, exceeding one meter in length, by the fact that the falling film is redistri¬ buted by means of at least two changes between ridge and valley along the plate length, i.e. by the fact that the falling film surface at least comprises three zones in the falling direction with intermediate redistribution between ridges and valleys. It is understood that the invention can be generally applied onto all types of falling film apparatuses of plate type like falling film coolers and falling film evaporators. In the case of falling film evaporators, besides the mentioned general advantages with area enlargement and supporting point arrange¬ ment, the corrugation pattern with valleys and ridges in the falling direction can also be utilized for bringing about evapo¬ ration channels with Increasing cross-section area and dimi¬ nishing heat transfer area in the falling direction. Such an evaporator is described in Swedish patent No. 424.143 of the applicant. Therefore, in the following the invention shall be further illustrated by a plate evaporator described by example with reference to the accompanying drawing, in which Fig . . 1 shows a schematical, partial view of a heat exchange plate according to the invention, Fig. 2 shows a partial view of a horizontal section through an upper part of a plate pile of a plate evaporator, Fig. 3 shows a partial view of a vertical section through a plate evaporator according to Fig. 2, and Fig. 4 shows a partial view of a further horizontal section through a lower part of the plate pile according to Fig. 2. Fig. 1 shows the principal design of a heat exchange plate 1 for a falling film heat exchanger according to the Invention, The plate 1 is corrugated such that ridges 2, 2', 2" and inter¬ mediate valleys 3, 3', 3", defined with regard to a falling film passage formed between the plate 1 and an adjacent plate, are formed in the falling film direction. The ridges 2 and the valleys 3 extend continuously within a zone Zγ like the ridges 2' and the valleys 3' within a successive zone Z« and the ridges 2" and the valleys 3" within a zone Z- j . In a transition zone T-,, between the zones Z-, and ∑2 a number of transi¬ tion surfaces 4 are formed, which connect the lower end of the ridges 2 in the zone Z-^ with the upper end of the valleys 3' in the zone Z - The transition surfaces 4 alternate in the cross-direction of the plate 1 with transition surfaces 5, which connect the lower end of the valleys 3 in the zone Z-^ with the upper end of the ridges 2' in the zone Z* , being understood that each of the alternate surfaces 4 and 5 forms a certain angle in its direction with regard to the falling direction. Corresponding transition surfaces 4' and 5' are formed in a transition zone T2 between the zones ~ and Z3 etc. It ought to be observed that the corrugation of the plate 1 ought not to contain sharp folds, but ridge tops and valley bottoms are suitably made with radii in the field of. size of 6-10 mm and the connection between the transition surfaces 4 and 5 and respective ridges and valleys ought to be made " with a radius exceeding 2 mm. Fig. 2-4 show how a number of plates formed according to the invention are oriented in relation to each other In a particular plate apparatus suitable for falling film evaporation. Two plates 10, 10' and 11, 11', respectively, which between them¬ selves form a falling film passage E, are oriented in relation to each other such that the ridges R, R' of one plate extend in alignment with the valleys of the other plate. The two plates 10, 11 and 10', 11', respectively, which between themselves form heat medium passages H, are oriented with their ridges, defined with regard to respective falling film passage, in alignment with each other. In the plate regions between the mentioned ridges, i.e. the regions forming ridges with regard to the heat medium passages, distance elements 12 are arranged. As is apparent from Fig. 3, each plate along its length is divided into zones Zι~Zg with intermediate transition zones T^-T^. In each transition zone a number of transition surfaces 13, 13', 14, 14' are arranged for connecting the ridges in one zone with the valleys in the consecutive zone and vice versa. It can be observed that adjacent transition surfaces 13, 13' in two plates 10, 10' forming a falling film passage E extend essentially parallel with each other. As is apparent from Fig. 3, the height of the ridge R'-R2~ R' -R Λ -R'e-Rg projecting into the evaporation passage E decreases in size from corresponding zone Zi-Zg indicated such that the cross-section area of the evaporation passage increases from zone to zone. As is best apparent from a compari- son between Fig. 2 and Fig. 4, due to that fact also the peri¬ meter of the evaporation passage E, wetted by the falling film, decreases from zone to zone. In Fig. 3 constant ridge height within each zone has been shown, but, of course, the ridge height can also successively decrease within each zone.

Claims: Claims 1. Heat exchanger of falling film type comprising heat exchange plates with area enlarging corrugation forming ridges and valleys extending in the falling film direction, c h a ¬ r a c t e r i z e d i n that the mentioned ridges (2, 2', 2") and valleys (3, 3', 3") extend continuously within each of a number of zones (Z-^, Z2, - j formed one after the other in the falling direction, that the ridges and the valleys of two consecutive zones are laterally displaced in relation to each other so that the ridges and the valleys, respectively, in one zone extend in alignment with the valleys and the ridges, res¬ pectively, in a consecutive zone, and that the corrugation of the plates in the transition passage (T-, , 2) between two consecutive zones forms connection surfaces (4, 4', 5, 5') for continuous liquid film flow from the lower end of the ridges and the valleys, respectively, in one zone to the upper end of the valleys and the ridges, respectively, in the consecutive zone. 2. Heat exchanger according to claim 1, c h a r a c t e r ¬ i z e d i n that the length of the plates in the falling film direction exceeds 1 m and comprises at least three of the mentioned zones. 3. Heat exchanger according to anyone of the preceding claims in which the heat exchange plates are arranged essentially ver¬ tically side by side and alternately delimit falling film pas¬ sages (E) for a fluid which is supplied like a falling film in the upper part of the mentioned passages and passages (H) for an additional medium that shall exchange heat with the mentioned falling film, c h a r a c t e r i z e d i n that two plates (10, 10') delimiting one of the mentioned falling film passages (E) are oriented with their ridges (R, R' ) and valleys, defined with regard to the falling film passage, such that the ridges of one plate extend in alignment with the valleys of the other plate. 4. Heat exchanger according to claim 3, c h a r a c t e r ¬ i z e d i n that the height of the mentioned ridges (R-Rg, R'-R'e) of two plates delimiting a falling film passage (E) decreases gradually or step by step in the falling film direc- tion such that the cross-section area of the falling film passage increases at the same time as the perimeter of the men¬ tioned cross-section area decreases in the mentioned direction. 5. Heat exchanger according to anyone of the preceding claims, c h a r a c t e r i z e d i n that the main part of each falling film passage (E) located inside the outer edges of the plates has no contact points or connection elements between the two plates (10, 10'; 11, 11') limiting the falling film passage. 6. Heat exchanger according to the claims 3-5, c h a r c ¬ t e r i z e d i n that two plates (10', 11; 10, 11') de¬ limiting a passage (H) for the mentioned additional medium are oriented with their respective ridges (R, R'), defined with regard to respective falling film passage (E), in alignment with each other, and that contact points or connection elements (12) between the two plates are arranged in the plate regions formed between the mentioned ridges (R, R').

Inventors: BOLMSTEDT ULF, LUNDBLAD BENGT, BOLMSTEDT, ULF, LUNDBLAD, BENGT
Applicants: ALFA LAVAL FOOD & DAIRY ENG, ALFA-LAVAL FOOD & DAIRY ENGINEERING AB
Application year: 1985
Main classification: F28F13
IPC codes: F28D3, F28D5, F28F3