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Publication numberUS2656885 A
Publication typeGrant
Publication dateOct 27, 1953
Filing dateFeb 16, 1949
Priority dateFeb 16, 1949
Publication numberUS 2656885 A, US 2656885A, US-A-2656885, US2656885 A, US2656885A
InventorsBurton S Hughes
Original AssigneeZaremba Company
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Concentrating apparatus
US 2656885 A
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Description  (OCR text may contain errors)

Oct. 27, 1953 Filed Feb. 16. 1949 B. S. HUGHES CONCENTRATING APPARATUS 2 Sheets-Sheet l M: Q -MJM ZSnven-l'or (Ittomeg Oct. 27, 1953 s. s. HUGHES CONCENTRATING APPARATUS 2 Sheets-Shoot Filed Feb. 16. 1949 Patented Oct. 27, 1953 2,656,885 CONOENTRATING APPARATUS Burton S. Hughes, Bufialo, N. Y., assignor to Zaremba Company, tion of New York Buffalo, N. Y., a corpora- Application February 16, 1949, Serial No. 76,730

4 Claims. 1

This invention relates generally to certain new and useful improvements in concentrators, but more particularly to a concentrating apparatus for evaporating water from fruit juices and like solutions which cause the coating of the heating surfaces with a slimy or gelatinous layer and interfere with the heat transfer unless continuously removed.

It is one of the objects of this invention to provide a concentrator of this character which is so designed and constructed as to provide for a high velocity of steam and vapor therethrough with a high rate of heat transfer and with less heating surface required for a given amount of evaporation.

Another object is to provide a concentrating apparatus which will effect concentration of the material in one pass therethrough and thereby prevent loss of valuable properties, particularlyin sensitive materials, due to the short time the material is in contact with the heating surfaces.

A further object of the invention is to provide a concentrator whose interior parts are so designed and arranged as to enable their ready withdrawal for cleaning.

Other features of the invention reside inthe construction and arrangement of parts hereinafter described and particularly pointed out in the appended claims.

In the accompanying drawings:

Figure 1 is a side elevation of the concentrating apparatus embodying my invention. Figure 2 is an enlarged fragmentary central longitudinal section thereof. Figure 3 is an end view of the same, viewing the left hand end of Figure 1. Figures 4 and 5 are cross sections taken substantially on the correspondingly numbered lines in Figure 2. Figure 6 is a longitudinal section taken on line 6-45, Figure 5. Figure 7 is an enlarged fragmentary cross section taken on line 'l-1, Figure 2, showing one of the scrapers for cleaning the inside surface of the steam jacket cylinder. Figure 8 is a fragmentary longitudinal section taken on line 8--8, Figure 7.

Similar characters of reference indicate corresponding parts throughout the several views.

In the preferred embodiment of the invention shown in the drawings, it comprises an outer stationary heating unit or steam jacketed cylinder I!) supported on suitable pedestals II, II, and an inner, slowly rotating cylinder 12 of substantially frusto-conical shape disposed therein and between the annular surfaces of which cylinders. the liquid to be concentrated is introduced and passed.

The steam jacketed cylinder I0 consists of an outer shell l3 and a concentrically-spaced inner shell I4 having helically-disposed ribs l5 therebetween providing a helical or spiral passage l6, closed at its ends, for the circulation of the steam which is introduced thereto through an inlet l1 located adjacent one end of such cylinder. This helical steam passage is gradually decreased in cross-sectional area from. its intake end in such proportion as to maintain a fairly uniform velocity of the steam. In its outer shell i3 this cylinder has a plurality of condensate drains I8, and in its top it has a vent I 9 for non-condensibles.

The inner rotatable cylinder [2 is tapered from the vent end of the stationary cylinder to its steam intake end and provided on its outer surface are helices or spiral ribs 26 which form a helical or spiral passage 2! for vapor between this rotating cylinder and the inner shell 14 of the companion cylinder. The ends of this passage are closed by walls 22, 23 and the wall 22 has a plurality of small intake ports 24 therein for the liquid to be concentrated while the opposite wall 23 has a plurality of larger outlet ports 25 therein. The ends of the rotating cylinder are closed by dished heads 23 having collars Z1 thereon and these collars are attached to a hollow shaft 28 extending axially through the cylinder and supported at its ends in suitable adjustable bearings 29 attached to heads 30, 3| applied to the extended end portions of the stationary cylinder I 0 and having stuifing boxes 32 disposed between the shaft and such heads. The head 30 is detachably connected to an end closure flange 33 applied to the some sponding end of the cylinder in while the companion head 3i may be fixed by welding or the like. A drive sprocket 34 is fixed on one end of this shaft for connection to a suitable source of power to impart a slow rotation to the inner cylinder 12.

The inner shell IA of the stationary or steamjacketed cylinder Ill is extended at one end beyond the tapered end of the rotating cylinder l2 to provide a vapor chamber 35 havmg a discharge passage 36 adapted for connection to a condenser. This chamber has a transverse partition or annular member 31 substantially centrally thereof to divide it into two parts and to prevent any of the concentrate discharged from the spiral passage 2| being carried out by the vapor. At the inner side of this partition the extended portion of this cylinder has a discharge opening 38 for the concentrate and at the opposite. or outer side thereof it has a drain 39 for removing the water while washing the interior of the apparatus. Between the opposing heads 26 and 30 there is provided a chamber into which the liquid to be concentrated is introduced through an inlet 4! formed in the head 30 and from which chamber the liquid is discharged through the ports 24 into the spiral passage 2| between the companion cylinders I!) and I2.

Disposed between and mounted on each pair of helices 2c is a scraping blade 42 in contact with the inner surface of the shell l4 ofthe steam jacket cylinder It to keep such surface clean of foreign matter during the rotation of the cylinder I2 and maintain the heat transfer into the spiral passage 2| at a maximum at all times. A light, substantially U-shaped spring 43 adjacent each end of the blade maintains it against the inner shell-surface, and the ends of the blade fit into a shallow notch 44 provided in the edges of adjoining helices with a milled slot 45 into which the edge of the scraper is inserted for holding it in place.

Extending through and beyond either end of the hollow shaft 28 is a beam 46, which may be of I-beam cross section, as shown in Figure 5, and which is supported at its opposite ends on vertically-adjustable pads 41 applied to companion jack-screws 43 mounted on frames 49. Trolleys 5e are arranged adjacent the ends of this hollow shaft, each including four wheels 5| in rolling contact with the base-flanges of the beam and two rollers 52 having their axes parallel with the axis of the shaft and adapted for contact with the inside of such shaft when the beam 46 is elevated. In the normal position of the parts shown in the drawings, with the beam lowered, the rollers 52 are free from contact with the hollow shaft 28 and it can turn freely. However, when the beam is raised by the jack-screws 43, these rollers contact the inner surface of the shaft and the inner assembly l2 of the concentrator and its associated parts can be removed from the outer assembly it for cleaning, as shown by dot-dash lines in Figure 1. The inner assembly can be rotated on the trolley-rollers 52 for convenience in washing and scrubbing the parts.

This apparatus is particularly useful in the evaporation of such products as fruit juices and the like which coat the heating surfaces with a slimy or gelatinous-like layer, and due to its structural arangement of parts and the high velocity of the steam and the vapor, the rates of heat transfer are high and a minimum of heating surface is required for a given amount of evaporation, all of which makes possible the concentration of the juice or solution in one pass through the concentrator without loss of valuable properties because of the short time it is in contact with the heating surfaces.

This apparatus, because of the ready removability of its interior parts for thorough cleaning, is also adaptable for evaporating water from milk or other solutions which must be concentrated under completely sanitary conditions. For such use the inner cylinder l2 can be stationary and need not be revolved.

I claim as my invention:

1. An apparatus of the character described, comprising an outer steam jacketed cylinder including helices therein. to define a spiral-like pausage for the steam and having end heads containing axial bearings, an inner tapered rotatable cylinder disposed axially of and in spaced relation to said outer cylinder for removal therefrom and to provide a forwardly-diverging annular passage adapted for communication at its converging intake end with the solution to be concentrated, said inner cylinder having helices on the exterior thereof extending through said annular passage from end to end thereof, and a hollow shaft extending axially of the inner cylinder and journaled at its ends in the head bearings of the outer cylinder and constituting a support for said cylinders, the outer cylinder having a chambered portion extending beyond the converging end of the inner cylinder and in communication with the diverging end of said passage and having a vapor ou let and a concentrate discharge therein, and an annular transverse partitionin said chamber separating said discharge from said vapor outlet.

2. An apparatus of the character described, comprising an outer cylinder having end heads one of which is removable, bearings applied axially of said heads, an inner revolvable cylinder disposed axially of and in spaced relation to said outer cylinder for removal therefrom, a hollow shaft extending axially of said inne cylinder and journaled at its end in the outer cylinder bearings, a beam extending through said shaft and adapted to be supported beyond the ends of the same, and trolley devices in said shaft including wheels in longitudinal guiding contact with said beam and rollers for contact with the inner surface of said shaft.

3. An apparatus of the character described, comprising an outer cylinder having end heads provided with bearings, one of said heads being removably mounted on such cylinder, a revolving cylinder removably arranged within said outer cylinder and including a hollow shaft extending at its ends through said end heads and journaled in the bearings thereof, a beam extending freely through said hollow shaft, vertically-adjustable supports for the ends of said beam, and trolley means disposed between the beam and the interior of said shaft and having wheels thereon for rolling contact with said beam and rollers normally out of contact with said shaft but adapted to contact the inner Wall thereof in an elevated position of the beam when removing the revolving cylinder from the outer cylinder.

4. A concentrating apparatus, comprising a horizontally-disposed cylindrical heating unit including inner and outer spaced shells having means in the annular space therebetween for circulating a heating medium therethrough in a helical path with the cross-sectional area of such path decreasing from one end thereof to the other to maintain a substantially uniform velocity of the heating medium, the outer shell having a plurality of openings therein for the continuous removal of the condensed heating medium, a

cylinder of substantially frusto-conical shape,

and closed at its ends, disposed axially within said heating unit in spaced relation thereto and having helices on its exterior surface defining a helical passage for the vaporizing of the solution to be concentrated, the helical pas-sage being closed at its ends and having intake ports at one end for the liquid to be concentrated and outlet ports at its opposite end and the cross sectional area of such passage increasing from its intake to its discharge end, the inner shell of said heatmg unit extending beyond the reduced end of the frusto-conical cylinder to provide a communicating vapor chamber having a concentrate discharge in its lower side and a vapor discharge in its upper side, and an annular partition disposed in said vapor chamber in a plane between the concentrate and vapor discharges to prevent the concentrated material being carried out by the vapor.

BURTON S. HUGHES.

References Cited in the file of this patent UNITED STATES PATENTS 10 Number Name Date Miller May 9, 1922 Mellott Mar. 16, 1926 Pezold Apr. 13, 1926 Rugh Oct. 8, 1929 Mortensen Apr. 19, 1932 Zorn et a1. Mar. 6, 1936 FOREIGN PATENTS Country Date Great Britain Feb. 5, 1894 Norway May 28, 1906

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US942407 *Dec 17, 1908Dec 7, 1909Charles OrdwayEvaporating apparatus.
US1164413 *Mar 16, 1915Dec 14, 1915Edward ShawApparatus for evaporating or concentrating liquids.
US1355702 *May 5, 1919Oct 12, 1920Edward ShawApparatus for evaporating or concentrating liquids
US1415255 *May 10, 1918May 9, 1922Evaporating And Drying MachineEvaporator
US1576838 *Feb 4, 1921Mar 16, 1926Mellott Howard SConcentrator
US1580164 *Jan 28, 1922Apr 13, 1926Pezold George JDrying apparatus
US1730902 *Jul 25, 1925Oct 8, 1929American Cyanamid CoMethod of and means for drying
US1854619 *Aug 28, 1930Apr 19, 1932Cornelius MortensenMilk treating apparatus
US2032785 *Jun 20, 1932Mar 3, 1936Low Temperature Proc CompanyMethod of and apparatus for disassociating the components of solutions and mixtures
GB189402498A * Title not available
NO15214A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3253643 *Mar 18, 1963May 31, 1966Gudheim Arne RHorizontally axised evaporator of the rotary wiped thin film type
US3261391 *May 20, 1964Jul 19, 1966Gudheim Arne RThin-film processing apparatus
US3292683 *Nov 12, 1963Dec 20, 1966Paul JanosfiaWiped falling film evaporator
US3357477 *Dec 23, 1966Dec 12, 1967Artisan IndThin film processing apparatus
US3372095 *Nov 5, 1964Mar 5, 1968Nester And Faust Mfg CorpSeparator
US5085410 *Dec 14, 1989Feb 4, 1992Jersey Nuclear-Avco Isotopes, Inc.Modular processing system
US5185757 *Oct 8, 1991Feb 9, 1993Jersey Nuclear-Avco Isotopes, Inc.Modularized replaceable vaporizer and extractor apparatus
EP2100649A1 *Mar 13, 2008Sep 16, 2009Buss-SMS-Canzler GmbHThin-film vaporiser
Classifications
U.S. Classification159/11.2, 159/25.1, 159/12, 159/6.3, 159/DIG.410
International ClassificationB01D1/22, A23L2/10
Cooperative ClassificationB01D1/228, Y10S159/41, A23L2/10
European ClassificationA23L2/10, B01D1/22D4