# US 9,518,779 B2 · Drying plant for particulate materials

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- Number: US 9,518,779 B2
- Document ID: US9518779B2
- Status: Granted
- Kind: B2
- Application number: 14/678,122
- Filed: 2015-04-03
- Published: 2015-10-08
- Granted: 2016-12-13
- Earliest claimed: 2014-04-04
- Assignees: Garbuio S.p.A.
- Applicants: GARBUIO S.p.A.
- Inventors: Mansueto Favaro
- Web page: https://patentgrep.com/patent/US9518779B2

## CPC

- F26B 3/08: so as to loosen them, e.g. to form a fluidised bed {("fluidised-bed" technique in general B01J8/24; centrifugal fluidised beds F26B7/007)}
- A24B 3/04: Humidifying or drying tobacco bunches or cut tobacco (A24B3/12 takes precedence)
- A61G 11/007: {by translating}
- A61G 11/009: {with hand insertion windows, e.g. in the walls}
- F26B 17/045: {the material on the belt being agitated, dispersed or turned over by mechanical means, e.g. by vibrating the belt, by fixed, rotating or oscillating elements}
- F26B 17/101: {the drying enclosure having the shape of one or a plurality of shafts or ducts, e.g. with substantially straight and vertical axis (F26B17/107 takes precedence)}
- F26B 17/103: {with specific material feeding arrangements, e.g. combined with disintegrating means}
- A61G 1/00: Stretchers
- F26B 2200/22: Tobacco leaves
- F26B: DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM (drying devices for combines A01D41/133; racks for drying fruit or vegetables A01F25/12; drying foodstuffs A23; drying hair A45D20/00; body-drying implements A47K10/00; drying household articles A47L; drying gases or vapours B01D; chemical or physical processes for dewatering or like separating liquids from solids B01D43/00; centrifugal apparatus B04; drying ceramics C04B33/30; drying yarns or fabrics in association with some other form of treatment D06C; drying frames for laundry without heating or positive air circulation, domestic laundry-or spin-driers, wringing or hot pressing laundry D06F; furnaces, kilns, ovens F27)
- A24B: MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A61G: TRANSPORT, PERSONAL CONVEYANCES OR ACCOMMODATION SPECIALLY ADAPTED FOR PATIENTS OR DISABLED PERSONS (appliances for aiding patients or disabled persons to walk A61H3/00); OPERATING TABLES OR CHAIRS; CHAIRS FOR DENTISTRY; FUNERAL DEVICES (embalming corpses A01N1/00)

## Abstract

Drying plant for particulate materials comprising: a drying duct which is provided with a substantially horizontal rectilinear starting section, a rectilinear ascending final section which extends upwards with a predetermined angle of inclination with respect to the vertical, and a curved intermediate section which connects the rectilinear starting section to the rectilinear final section; a hot gas generator designed for supplying to the inlet of the rectilinear starting section of the drying duct a flow of process gas at high temperature; a particulate feeding device which is structured so as to be able to feed/introduce into the rectilinear starting section of the drying duct a flow of particulate material to be dried substantially without relevant leaks of process gas from the drying duct; and a bypass duct which branches from the rectilinear starting section of the drying duct upstream of the particulate feeding device, and then re-joins the drying duct at the curved intermediate section, so as to feed back into the drying duct the process gas diverted inside it.

## Claims

### Claim 1

A drying plant for particulate materials comprising: an ascending drying duct, a hot gas generator designed for supplying to the inlet of the drying duct a flow of high-temperature process gas, and a particulate feeding device structured so as to be able to feed into the drying duct a flow of the particulate material to be dried substantially without relevant leaks of process gas from the drying duct;
wherein the drying duct has a substantially rectilinear and substantially horizontal starting section, a substantially rectilinear ascending final section extending upward with a predetermined angle of inclination with respect to the vertical, and an intermediate curved section that connects the starting section to the final section;
wherein the hot gas generator is connected to the mouth of the starting section of the drying duct;
wherein the particulate feeding device is located along the starting section of the drying duct, at a predetermined distance from the curved intermediate section; and in that
wherein it also comprises a bypass duct that branches from the starting section of the drying duct upstream of the particulate feeding device, and then rejoins the drying duct at the intermediate curved section, so as to feed the process gas that flows therein back into the drying duct.

### Claim 2 (depends on 1)

Drying plant according to claim 1, wherein the bypass duct connects/joins to the intermediate curved section of the drying duct at the wall of the drying duct arranged outside of the bend.

### Claim 3 (depends on 1)

Drying plant according to claim 1, wherein the bypass duct is structured so as to feed, at the intersection with the intermediate curved section, the process gas into the drying duct in a direction which is inclined by a predetermined angle with respect to the direction of the flow of process gas which arrives from the starting section of the drying duct.

### Claim 4 (depends on 3)

Drying plant according to claim 3, wherein the bypass duct is structured so as to feed, at the intersection with the intermediate curved section, the process gas into the drying duct so as to push the particles of particulate material suspended in the flow of process gas upwards in a predetermined direction.

### Claim 5 (depends on 4)

Drying plant according to claim 4, wherein the end part of the bypass duct is structured so as to feed the process gas into the intermediate curved section of the drying duct in a direction that is inclined with respect to the vertical by an angle ranging between 0° and 45°.

### Claim 6 (depends on 4)

Drying plant according to claim 4, wherein said predetermined direction is locally substantially parallel to the longitudinal axis of the final section of the drying duct.

### Claim 7 (depends on 6)

Drying plant according to claim 6, wherein the end part of the bypass duct is structured so as to feed the process gas into the intermediate curved section of the drying duct in a direction that is oriented so that the sum of the velocity vector of the process gas coming from the bypass duct and the velocity vector of the process gas coming from the starting section of the drying duct gives rise to a velocity vector oriented so as to be locally substantially parallel to the longitudinal axis of the final section of the drying duct.

### Claim 8 (depends on 5)

Drying plant according to claim 5, wherein the bypass duct connects to the intermediate curved section of the drying duct at the end of a curved portion which is structured so as to feed the process gas into the intermediate curved section in a direction which is inclined with respect to the vertical by an angle ranging between 0° and 45°.

### Claim 9 (depends on 1)

Drying plant according to claim 1, wherein the particulate feeding device is located along the starting section of the drying duct, at a distance greater than one meter from the curved intermediate section.

### Claim 10 (depends on 1)

Drying plant according to claim 1, wherein the starting section of the drying duct is structured so as to generate, at the particulate feeding device, a sudden decrease in the process-gas pressure which tends to suck the particulate material toward the curved intermediate section of the drying duct.

### Claim 11 (depends on 1)

Drying plant according to claim 1, further comprising an airflow control device which is located inside the bypass duct and/or inside the starting section of the drying duct, and is structured so as to be able to regulate the flow rate of the process gas that flows along the bypass duct and/or the flow rate of the process gas that flows along the part of the starting section of the drying duct located downstream of the branch.

### Claim 12 (depends on 1)

Drying plant according to claim 1, wherein inside the bypass duct there are located one or more longitudinal septums which extend parallel to the centerline of the bypass duct and are orthogonal to the lying plane of the bypass duct.

### Claim 13 (depends on 1)

Drying plant according to claim 1, further comprising one or more movable flow deflector devices each of which is located inside the bypass duct at the intersection with the intermediate curved section of the drying duct, and is structured so as to be able to vary, as a function of its own position, the direction of the process gas entering the intermediate curved section of the drying duct.

### Claim 14 (depends on 1)

Drying plant according to claim 1, wherein the ascending final section of the drying duct extends upward with an angle of inclination with respect to the vertical ranging between 0° and 30°.

### Claim 15 (depends on 1)

Drying plant according to claim 1, further comprising a centrifugal dust separator which is connected to the mouth of the final section of the drying duct so as to receive at the inlet the process gas with the suspended particles of particulate material, and is structured so as to make the particles of particulate material precipitate therein, while discharging the process gas from a gas outlet.

### Claim 16 (depends on 15)

Drying plant according to claim 15, wherein the centrifugal dust separator is a cyclone filter which is connected to the mouth of the final section of the drying duct so as to receive at the inlet the process gas with the suspended particles of particulate material, and is structured so as to cause the particles of particulate material to precipitate on the bottom of the cyclone filter, while discharging the process gas from a gas outlet preferably located on top of the cyclone filter.

### Claim 17 (depends on 16)

Drying plant according to claim 16, wherein the cyclone filter is provided with a particulate extraction device which is located on the bottom of the cyclone filter and is structured so as to allow removal, from the cyclone filter, of the particles of particulate material that deposit on the bottom of the cyclone filter substantially without relevant leaks of process gas from the cyclone filter.

### Claim 18 (depends on 1)

Drying plant according to claim 1, wherein the hot gas generator is structured so as to supply to the inlet of the drying duct a process gas with a temperature greater than 150° C.

### Claim 19 (depends on 1)

Drying plant according to claim 1, wherein the particulate feeding device is structured so as to be able to feed, into the drying duct, a flow of particles of cut tobacco to be dried.