Apparatus for wetting and dissolving dry particles

• US 5,253,578 A
• Filed: 03/16/1992
• Issued: 10/19/1993
• Est. Priority Date: 03/16/1992
• Status: Expired due to Fees

• Current Assignee: Nestec SA (Nestle SA)
• Original Assignee: Nestec SA (Nestle SA)
• Inventors: Hsu, Sheng H.
• Primary Examiner(s): Simone, Timothy F.
• Application Number:
  US07/852,054
• Time in Patent Office: 582 Days
• Field of Search: 99/516, 99/534, 99/536, 99/471, 99/474, 99/483, 99/484, 99/275, 99/283, 99/287, 99/348, 141/67, 141/105, 222/272, 222/312, 222/129.2, 241/101.8, 366/172, 366/177, 366/182, 366/154, 366/165, 366/167, 366/168, 366/187, 366/290, 366/292, 366/297, 366/300, 426/433, 426/434, 426/427, 426/478
• US Class Current: 99/275
• CPC Class Codes: B01F 21/00 Dissolving separating by dissolving B01D; dissolving to effect cooling F25D5/00
• CPC Class Codes: B01F 21/10 using driven stirrers
• CPC Class Codes: B01F 21/15 comprising constructions for blocking or redispersing undissolved solids, e.g. sieves, separators or guiding constructions B01F21/221 takes precedence
• CPC Class Codes: B01F 25/85 wherein the particles fall onto a film that flows along the inner wall of a mixer
• CPC Class Codes: B01F 27/74 with rotary cylinders
• CPC Class Codes: B01F 33/8212 with moving and non-moving stirring devices

Abstract

This invention is directed to an apparatus and method for wetting and dissolving finely divided dry particles, including hygroscopic particles such as coffee fines, in a liquid, including viscous liquids such as concentrated coffee liquor, in a manner in which foaming, the presence of wet lumps and liquor degradation are minimized. The apparatus includes a dissolving tank containing at least one pair of counter-rotating drums partially submerged in a body of the dissolving liquid. The tank includes a liquid inlet and a discharge conduit which maintain a predetermined level of liquid in the tank. A powder feeding device mounted above the tank discharges a falling curtain of particles onto a thin layer of liquid on the surface of one of the drums in each counter-rotating pair. The partially wetted powder is carried into the nip between the counter-rotating drums to compress, knead and break up wet lumps of partially wetted powder formed on the surface of the drums, with the wetted powder being carried into and dissolved in the body of liquor. Continued rotation of the drums carries any wet powder lumps which may remain in the liquor into the converging gap between the drum and a tangentially mounted solubilizing bar to abrade and disintegrate the lumps in the liquor body.

Claims

1. An apparatus for wetting and dissolving finely divided dry particles in a liquid which comprises

a dissolving tank having liquid supply means and discharge means, gate means in said tank intermediate said supply means and discharge means to provide a body of liquid of predetermined level in said tank,

at least one pair of axially aligned counter-rotating drums mounted in said tank partially submerged in said body of liquid, the drums in each of said pair being mounted in close proximity to define a nip therebetween,

means for rotating each drum in each of said counter-rotating pairs toward said nip,

a solubilizing bar tangentially mounted substantially parallel and in close proximity to an upwardly rotating section of each drum submerged in the body of liquid, said bar extending over substantially the entire axial length of the drum to provide a converging gap between the bar and the surface of the adjacent drum,

feeding means mounted above the dissolving tank for depositing the dry particles onto one of the drums in each counter-rotating pair, and

filter means in communication with the liquid discharge means of said tank to receive liquid from the tank and disintegrate and dissolve any solid particles in the liquid.

2. The apparatus defined in claim 1 in which the gate means comprises an adjustable flow gate mounted across the dissolving tank adjacent one end thereof to maintain a level of liquor in said tank sufficient to partially submerge said drums.

3. The apparatus defined in claim 1 in which two pairs of counter-rotating drums are mounted in the tank, with the drums in both pairs of drums being mounted in close proximity and being rotated in a direction toward the nip between the drums.

4. The apparatus defined in claim 3 in which the nip between the drums in both pairs of drums is between about 6 mm to 12 mm in width.

5. The apparatus defined in claim 3 in which the dry particles are deposited over substantially the entire axial length of one of the drums in each counter-rotating pair.

6. The apparatus defined in claim 5 in which the liquid supply means includes distribution conduits mounted above the drums to distribute liquid onto the surface of one of the drums in each counter-rotating pair over substantially the entire axial length of the drums.

7. The apparatus defined in claim 3 in which a solubilizing bar is mounted adjacent each of the drums, with each solubilizing bar being positioned tangential to an upwardly rotating section of the adjacent drum.

8. The apparatus defined in claim 1 in which said filter means comprises a plurality of wedge elements secured in close proximity to one another in a coplanar relationship at the base of the wedges and formed into a cylindrical shape, with the base of the wedges forming the outer surface of the filter and the apex of the wedges forming the inner surface of the filter to define a converging gap between adjacent wedges.

9. The apparatus defined in claim 3 in which said feeding means includes a hopper for storing dry particles, said hopper having an outlet for discharging the dry particles, a metering roller mounted adjacent and below said outlet to control the rate of particle discharge from the hopper, a vibrating inclined feed tray means mounted under the metering roller to receive dry particles discharged from the metering roller, with the end of the feed tray means remote from the metering roller being positioned to deposit a curtain of dry particles over substantially the entire axial length of one of said drums in both counter-rotating pairs.

10. The apparatus defined in claim 9 in which said feed tray means includes a first inclined feed tray having an inlet end mounted below said metering roll and a discharge end positioned above a drum in one of the pair of counter-rotating drums in the dissolving tank, and a second inclined feed tray mounted on the bottom surface of said first feed tray adjacent the discharge end thereof and extending in a direction opposite to that of the first feed tray, with said second feed tray having a discharge end positioned above a drum in the other pair of counter-rotating drums, said first feed tray having a plurality of spaced openings across the width of the tray above said second feed tray, whereby a portion of the dry particles carried on the first feed tray fall through said openings onto the second feed tray and are discharged therefrom, with the remainder of the dry particle passing between the spaced openings and being discharged from the end of the first feed tray.

11. The apparatus defined in claim 10 in which the openings in the first feed tray are spaced apart a distance at least equal to the width of the openings.