Method and apparatus for drying particulate material

• US 5,406,718 A
• Filed: 01/04/1994
• Issued: 04/18/1995
• Est. Priority Date: 01/04/1994
• Status: Expired due to Fees

• Current Assignee: Grana Incorporated
• Original Assignee: Grana Incorporated
• Inventors: Stein, Peter
• Primary Examiner(s): ESQUIVEL, DENISE LYNNE
• Application Number:
  US08/177,015
• Time in Patent Office: 469 Days
• Field of Search: 34/370, 34/361, 34/362, 34/587, 34/579, 34/589, 34/594, 34/406, 34/403, 34/168, 34/171, 34/178, 110/245, 432/58, 122/4 D, 422/139, 422/141, 422/143, 165/104.16
• US Class Current: 34/362
• CPC Class Codes: F26B 17/1458 consisting of perforated panels or baffles; consisting of grids
• CPC Class Codes: 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

Abstract

The present invention relates to a method and apparatus for drying particulate materials such as seeds and grains in which an air dryer having at least one drying stage is accompanied by means to create an upwardly vertical air flow having a velocity in the mesh openings at least equal or larger than the suspension speed of the particles to be dried so that they are temporarily suspended until enough accumulate to provide sufficient weight or downward pressure for the particles to overcome the upward air flow, pass downward through one or more mesh screens and reach the bottom of the dryer. The present invention also relates to a method and apparatus for effecting chemical and/or physical reactions.

Claims

1. An air dryer for drying particle formed materials comprising:

a housing having a top, bottom and substantially parallel side walls and defining an interior having a substantially uniform cross-section in the vertical direction;

means for introducing materials to be dried into said housing;

at least one drying stage having mesh means defining openings greater than the largest size particle of the material to be dried, said drying stage located between the top and bottom walls and extending to the side walls of said housing;

means for introducing air into each drying stage;

air flow means for extracting air from the top of said housing and for a subatmospheric pressure and a rotating and upwardly vertical flow of air within said housing having a velocity within the mesh openings at least equal to the speed at which the material to be dried remains suspended, and for suspending the particles above the mesh means to provide sufficient weight or downward pressure for the particles to overcome the upward air flow, pass through the openings in the mesh means and fall to the bottom of said housing.

2. An air dryer according to claim 1, wherein said means for introducing materials comprises a plurality of concentric distribution cones to distribute said materials over a horizontal plane of an uppermost drying stage, and wherein the cones are made of mesh material having a clearance smaller than the particle material to be dried.

3. An air dryer according to claim 1, wherein said means for introducing materials comprises a distributor at the top of the housing and wherein the housing increases in diameter at the top.

4. An air dryer according to claim 1, wherein said means for introducing air into each drying stage introduces air in a rotating pattern.

5. A method for drying particle formed materials comprising the steps of:

loading particle formed materials to be dried into the top of a housing of a dryer having a top, bottom and substantially parallel side walls to define an interior having a substantially uniform cross-section in the vertical direction, and at least one drying stage having a mesh means defining openings slightly greater than the largest size particles to be dried, said drying stage located between the top and bottom walls and extending to the side walls of the housing; and

introducing air into each drying stage; and

extracting air from the top the housing to create a subatmospheric pressure and a rotating and upward air flow in said housing having a velocity within the mesh openings at least equal to the suspension speed of particles to be dried, whereby particles to be dried will remain suspended until enough particles accumulate above the mesh means to provide sufficient weight or downward pressure for the particles to overcome the upward air flow, pass through the openings in the mesh means and fall to the bottom of said housing.

6. An apparatus for effecting chemical and physical reactions by means of a solid/gas contact comprising:

a housing having a top, bottom and substantially parallel side walls and defining an interior having a substantially uniform cross-section in the vertical direction;

means for introducing solid particle materials having a defined particle size into said housing;

at least one interaction stage having mesh means defining openings slightly greater than the particle size of the material, said interaction stage located between the top and bottom walls and extending to the side walls of said housing;

gas flow means for extracting gas from the top of said housing and for creating a subatmospheric pressure and a rotating and upwardly vertical flow of gas within said housing having a velocity within the mesh openings at least equal to the speed at which the material remains suspended, and for suspending the particles above the mesh means until enough particles accumulate above the mesh means to provide sufficient weight or downward pressure for the particles to overcome the upward gas flow, pass through the openings in the mesh means and fall to the bottom of said housing.

7. A method for effecting chemical and physical reactions by means of a solid/gas contact comprising:

loading particle formed solid materials having a defined particle size into the top of a housing having a top, bottom and substantially parallel side walls to define an interior having a substantially uniform cross-section in the vertical direction, and at least one interaction stage having a mesh means defining openings slightly greater than the particle size of the material, said interaction stage located between the top and bottom walls and extending to the side walls of the housing; and

extracting gas from the top of the housing and for creating a subatmosphere pressure and a rotating and an upward gas flow in said housing having a velocity within the mesh openings at least equal to the suspension speed of particles, to suspend the particles until enough particles accumulate above the mesh means to provide sufficient weight or downward pressure for the particles to overcome the upward gas flow, pass through the openings in the mesh means and fall to the bottom of said housing.