U.S. patent number 3,647,188 [Application Number 05/022,640] was granted by the patent office on 1972-03-07 for airlift blending apparatus.
This patent grant is currently assigned to Fuller Company. Invention is credited to Paul E. Solt.
United States Patent |
3,647,188 |
Solt |
March 7, 1972 |
AIRLIFT BLENDING APPARATUS
Abstract
A blending apparatus for mixing dry powdered materials
consisting of an upright silo with a gas-permeable divider and a
gas supply providing fluidizing gas up through the divider. A
hollow blending column, open at its top and bottom, is vertically
mounted in the silo with its bottom end spaced from the
gas-permeable divider and gas is directed upwardly through the
blending column at a velocity higher than the fluidizing gas
velocity in the silo to circulate material from the silo upwardly
through the blending column.
Inventors: |
Solt; Paul E. (Allentown,
PA) |
Assignee: |
Fuller Company (N/A)
|
Family
ID: |
21810637 |
Appl.
No.: |
05/022,640 |
Filed: |
March 25, 1970 |
Current U.S.
Class: |
366/107;
366/173.1 |
Current CPC
Class: |
B01F
13/025 (20130101) |
Current International
Class: |
B01F
13/02 (20060101); B01F 13/00 (20060101); B01f
013/02 () |
Field of
Search: |
;259/4,18,DIG.17,1,95 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
543,647 |
|
Dec 1955 |
|
BE |
|
539,141 |
|
Nov 1931 |
|
DD |
|
Primary Examiner: Jenkins; Robert W.
Claims
I claim:
1. A blending system for dry pulverulent material comprising an
upright vessel with a material inlet port and a material outlet
port, a gas-permeable divider positioned in the vessel dividing the
vessel into a material chamber and a lower plenum chamber, said gas
permeable divider being in the general form of an inverted
truncated cone, at least one blending column vertically mounted
inside said vessel and extending upwardly from said divider, said
blending column being hollow and open at its top and bottom with
the bottom being spaced from the divider to provide a
material-intake opening into the blending column, fluidizing gas
means in fluid flow communication with the vessel for supplying
fluidizing gas to the material chamber through the divider, and
blending gas supply means adapted to supply gas into the bottom of
the blending column at a velocity higher than that of the
fluidizing gas supplied to the material chamber.
2. The apparatus of claim 1 in which a plurality of blending
columns are mounted in said vessel.
3. The apparatus of claim 2 in which said blending columns
terminate at different heights above the gas-permeable divider.
4. The apparatus of claim 2 wherein the blending columns contain
openings positioned along their length.
5. The apparatus of claim 3 wherein the blending columns contain
openings positioned along their length.
6. The apparatus of claim 1 wherein the material outlet port is
located in the upper portion of the upright vessel.
Description
BACKGROUND OF THE INVENTION
This invention relates to bulk blending apparatus for the mixing
and blending of dry pulverulent materials. Materials to be blended
are usually introduced into a suitable bin or vessel. It is
essential that the various materials be completely intermingled and
mixed prior to being discharged from the vessel. This invention is
concerned more specifically with the blending of dry powdered
materials that are not free-flowing and which require fluidization,
such as cement raw materials.
Various means have been employed to achieve the aforementioned
blending of materials. The blending of mixtures of dry powdered
fluidizable materials is frequently accomplished by introducing a
diffused flow of gas through the material to produce a fluidized
condition of the air-material mixture. Blending can thus be
accomplished in a vessel with a porous bottom through which the
fluidizing gas is diffused and introduced into the powdered
material. By adjusting the velocity of gas through the material it
is possible to introduce various degrees of turbulence and as a
consequence, various rates and completeness of blending within the
vessel.
A further improvement of the aforementioned type of apparatus is
disclosed in U.S. Pat. No. 3,003,752 and U.S. Pat. No. 2,844,361
and includes a vessel provided with a gas-permeable floor. The
gas-permeable floor is separated into quadrants with means provided
for individually varying the amount of airflow through a selected
quadrant. In this way, increased airflow through a given quadrant
will decrease the density of the air-material mixture above the
more active quadrant thereby reducing the pressure of the material
over this quadrant. The material over the more active quadrant
rises upwardly and flows over the top of the fluidized material in
the less active adjacent quadrants. Furthermore, the more dense
material in the less active quadrants flows inwardly to replace the
less dense material in the active quadrant thereby promoting the
blending action. As the diameter and height of the blending
receptacle are increased, the delineation of the active zone
becomes less distinct. This, of course, reduces the blending
efficiency of the apparatus.
It is, therefore, an object of this invention to create a
well-defined and controlled column of a reduced density of
gas-material mixture in a fluidized mass of material which will
increase circulation of material and thereby increase blending
efficiency.
SUMMARY OF THE INVENTION
This invention relates to a blending system for dry pulverulent
material comprising an upright vessel with a material inlet port
and a material outlet port, a gas-permeable divider positioned in
the vessel and dividing the vessel into an upper material chamber
and a plenum chamber, at least one blending column vertically
mounted inside said vessel, said blending column being hollow and
open at its top and bottom with the bottom being spaced from the
divider to provide a material intake opening into the blending
column, fluidizing gas means in fluid flow communication with the
plenum chamber for supplying fluidizing gas to the material chamber
through the divider, and blending gas supply means adapted to
supply gas into the bottom of the blending column at a velocity
higher than that of the fluidizing gas supplied to the material
chamber. A plurality of blending columns can be used and the
columns can be varied in height and/or can have openings positioned
along their length to create intermixing at various levels of the
material.
BRIEF DESCRIPTION OF THE DRAWINGS
In the drawings:
FIG. 1 is a sectional view of a blending apparatus of the present
invention;
FIG. 2 is a sectional view of an alternate embodiment of the
invention;
FIG. 3 is a sectional view of a modified form of blending chamber
of the apparatus of FIGS. 1 or 2 having openings in the walls
thereof; and
FIG. 4 is a modification of the apparatus of FIG. 1 having a
material discharge port located in the upper portion of the
material chamber.
DETAILED DESCRIPTION
Referring to the drawings, the blending system comprises an upright
vessel or bin 10 such as a large outdoor storage silo for cement
raw materials having a circular side wall 14 with a material inlet
port 12 at its upper end and a material outlet port 13 at its lower
end. The material discharge port 13 is connected to a discharge
conduit 15 having a cutoff valve 16 therein to control material
discharge from the bin. Spaced from the bottom 17 of the bin 10 is
a gas-permeable divider 18 which divides the bin into an upper
material chamber 27 and a lower plenum chamber 19. The divider 18
slopes from all points on the upper surface thereof toward the
material outlet port 13. Thus the divider of FIG. 1 is an inverted
truncated cone and that of FIG. 2 is a sloping trough. The divider
18 may be comprised of any suitable gas-permeable medium such as
porous stones, fabric or perforated metal and overlies the plenum
chamber 19. A gas conduit 20 delivers gas under pressure, suitably
air for inert materials, to the plenum chamber 19 to provide
fluidizing air for the material chamber 27. An advantage of the
truncated cone-shaped divider 18 is that it assists the flow of
material along the upper surface of the divider toward the blending
column thus eliminating segregation of the material. This is
particularly important in the modification of FIG. 4 in which the
cutoff valve 16 is closed and the blender operates continuously
with the material discharging through a material discharge conduit
15' located in the upper portion of the material chamber 27. In
this arrangement of FIG. 4, the material conduit 15' acts like a
material overflow to discharge material in a continuous operation.
The cutoff valve 16 is then used as a cleanout valve for removing
oversized particles from the material chamber. Like parts of the
apparatus of FIG. 4 have the same numerals as FIG. 1 and operate in
the same manner as described with reference to FIG. 1.
A hollow blending column 21 in the form of a cylindrical tube or
casing and open at its top and bottom and having a funnel-shaped
bottom 23 is mounted vertically in the vessel 10. The blending
chamber 21 is connected to the vessel by connecting means, such as
metal rods 22, and the lower end of the chamber is spaced from the
divider 18 to provide a material intake opening 28. Nozzles 24
receive gas from the gas conduit 20 and direct a higher velocity
gas into the blending column 21. This higher velocity gas has a
greater lifting action than the fluidizing air passing through the
gas-permeable divider 18, thereby creating a less dense column of
material in the column 21. The less dense column is displaced
upwardly through the column 21 by the more dense material flowing
into the chamber through intake opening 28.
In FIG. 2 is shown a form of the invention in which a plurality of
blending columns 21' of varying heights are mounted in the material
vessel by supports (not shown) in a manner similar to the chamber
21 in FIG. 1. The varying heights permit discharge of material at
different levels, thus creating intermixing of different levels of
material. The columns may, of course, be of the same height. In
this form of the invention a separate gas conduit 26 is utilized
for supplying the blending gas to the nozzles 24. This permits
better control of the velocities of the fluidizing gas supplied by
gas conduit 20 and blending gas supplied by conduit 26. One
velocity can be modified without directly affecting the other, thus
permitting rapid adjustments that may be necessary due to the
condition of or type or material to be blended.
In FIG. 3 is shown a modified form of blending column of the type
shown in FIGS. 1 and 2, but containing a plurality of openings 25
through its wall at various elevations. These openings permit
partial flow of material into and out of the blending column at
various levels, thereby intermingling the material in the column
with materials at various levels in the material chamber 27. It
will be understood that the openings may be only at the top, or
bottom, or any combination of positions of the column dependent
upon the blending conditions desired.
The operation of the assembly is largely evident from the foregoing
description. A low volume of air is supplied into the plenum
chamber 19 of the vessel 10 to provide fluidizing air to pass up
through the divider 18 and into the vessel 10. Fluidizing air at a
substantially higher volume is directed into the blending column 21
or 21' for expanding material in the chamber. The expanded material
column in the column is less dense, and therefore, has
less-pressure head than the surrounding material in the material
chamber 27. A material flow pattern is thereby established with the
high-pressure material surrounding the vertical blending column
flowing toward and into the bottom of the blending column and being
displaced upwardly through the chamber and out through the top of
the column and across the top of the material in the vessel, as
shown by the arrows. This creates a continuous and rapid
circulation of material upwardly through the column despite the
fluidized mass of material in the chamber 27, and produces a rapid
blending action which accomplishes the blending operation in a
shorter period of time and with a reduced total air requirement.
The degree of mixing, as noted, can be varied by the provision of
additional vertical columns disposed within the vessel, by making
the columns of different heights, thus providing discharge zones at
different levels in the vessel thereby creating mixing of different
levels within the vessel, and by providing the column or columns
with openings at various points along their length which permits
partial flow of material into and out of the column at various
elevations.
It will be understood that is is intended to cover all changes and
modifications of the disclosure of the invention herein chosen for
the purpose of illustration which do not constitute departures from
the spirit and scope of the invention.
* * * * *