U.S. patent number 3,751,009 [Application Number 05/231,140] was granted by the patent office on 1973-08-07 for motionless mixing device.
This patent grant is currently assigned to Joseph P. McHugh. Invention is credited to Stephen V. Archer.
United States Patent |
3,751,009 |
Archer |
August 7, 1973 |
MOTIONLESS MIXING DEVICE
Abstract
A motionless mixing device in which a hollow, cylindrical tube
has fixedly positioned within the tube a plurality of mixing
elements in end-to-end contact, wherein each mixing element
comprises a flat, generally rectangular plate-like member having a
pair of flat, plate-like vanes mounted substantially perpendicular
on opposite faces of the plate-like member, the vanes in each pair
being angled in opposite directions, the angle between any pair of
adjacent plate-like members being about 90.degree.. An apertured
disk may be positioned between the mixing elements to improve
transverse flow. BACKGROUND OF THE INVENTION This invention relates
to a new and improved motionless mixing device, that is, to a
mixing device in which the mixing elements remain stationary during
the mixing operation. More particularly, the invention relates to
motionless mixing devices of the mechanical type rather than
motionless mixing devices primarily based upon the application of a
nonmechanical external force as in sonic or magnetic mixing. The
advantages of motionless mixing over mechanical dynamic mixing are
well appreciated. These advantages include more efficient use of
external material-transferring devices such as pumps and the like,
since motionless mixers are not wasteful of power requirements as
are dynamic mixers when the viscosity of the material being mixed
is initially high or increases during the mixing operation.
Moreover, motionless mixers normally can be engineered to suit the
particular materials being admixed, in terms of the dimensions and
number of mixing elements and the like. Motionless mixers also
avoid the undesirable heat, shear and vibration often generated by
mixers having moving elements, and motionless mixers require only a
minimum of maintenance. One problem of motionless mixers, however,
has been excessive pressure drop as material is passed through the
mixer. It is evident that if the flow rate of the material through
a mixing device falls off rapidly as the material moves from the
inlet to the outlet, the device will be inefficient for many
applications even though it provides good mixing. This problem has
at least been partially solved by mixing devices in which the
mixing elements are helical in configuration, as in U.S. Pat. No.
3,286,992 -- Armeniades et al. However, while solving the problem
of pressure drop, the known motionless mixing devices remain
deficient in other respects. For example, the helical mixing
elements of the foregoing patent require very careful tooling in
order to provide the proper twist. This adds substantially to the
expense of the completed mixing device and makes it uneconomical to
use the device for many relatively commonplace mixing operations.
Another problem is the lack of usefulness of the known motionless
mixing devices for certain mixing applications, such as the
aeration of sludge. Even when the mixing device can be adapted to a
wider range of mixing applications, the adaptation requires major
redesigning of the device and the resulting costs often make the
adaptation uneconomical. OBJECTS AND SUMMARY Accordingly, an object
of the invention is to provide a new and improve motionless mixing
device wherein the mixing elements and other structural elements
are simple and easily constructed, such that the cost of the
completed device is low in comparison with known motionless mixing
devices. Another object is to provide a new and improved motionless
mixing device which is useful without adaptation to a wide variety
of mixing operations or, if adaptation is required, the adaptation
is easily and inexpensively achieved. Still another object of the
invention is to provide a new and improved motionless mixing device
which is substantially more efficient in providing aeration of
materials when this result is desirable, as in the digestion of
sewage or sludge by the bubbling of air therethrough. These and
other objects, features and advantages of the invention will be
apparent from the specification which follows. In summary outline,
these and other objects are achieved by a motionless mixing device
in which a plurality of mixing elements are fixedly positioned
substantially end-to-end within a hollow, cylindrical tube having
an inlet and an outlet for passage of material through the tube.
Each mixing element comprises a flat, generally rectangular
plate-like member having a pair of flat, plate-like vanes mounted
substantially perpendicular on opposite faces of the plate-like
member, the vanes in each pair being angled in opposite directions,
the angle between any pair of adjacent plate-like members being
about 90.degree.. An apertured disk may be positioned between any
of the mixing elements to improve transverse flow. The invention
accordingly comprises the features of construction, combination of
elements, and arrangement of parts which will be exemplified in the
construction hereinafter set forth, and the scope of the invention
will be indicated in the claims.
Inventors: |
Archer; Stephen V. (Hamden,
CT) |
Assignee: |
McHugh; Joseph P. (Hamden,
CT)
|
Family
ID: |
22867898 |
Appl.
No.: |
05/231,140 |
Filed: |
March 2, 1972 |
Current U.S.
Class: |
366/337 |
Current CPC
Class: |
B01F
25/43161 (20220101) |
Current International
Class: |
B01F
5/06 (20060101); B01f 005/00 () |
Field of
Search: |
;259/4,18,36,DIG.30,180 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Jenkins; Robert W.
Claims
What is claimed is:
1. In a motionless mixing device, the combination of a hollow
cylindrical tube having an inlet and an outlet, and a plurality of
mixing elements fixedly positioned within said tube; each of said
mixing elements comprising a flat, generally rectangular plate-like
member having a pair of flat, plate-like vanes mounted
substantially perpendicular on opposite faces of said member, the
vanes in each said pair being angled in opposite directions, said
mixing elements being aligned substantially end-to-end within said
tube such that the angle between any adjacent plate-like members is
about 90.degree. .
2. A mixing device as in claim 1 further including a plurality of
disks separating some of said plate-like members, said disks being
co-axial with the longitudinal axis of said tube and having at
least one aperture therethrough for relief of pressure.
3. A mixing device as in claim 2 wherein every other of said
plate-like members is separated by one of said disks.
4. A mixing device as in claim 2 wherein all adjacent plate-like
members are separated by one of said disks.
5. A mixing device as in claim 2 wherein the diameter of said disks
is from about one-fourth to about three-fourths of the internal
diameter of said tube.
6. A mixing device as in claim 1 wherein the length of said
plate-like member is greater than its width, and the leading edge
of said member is adapted for the slicing of solid material
entering said tube.
7. A mixing device as in claim 6 wherein said leading edge is
rounded.
8. A mixing device as in claim 6 wherein said leading edge is a
knife edge.
9. A mixing device as in claim 6 wherein said leading edge is
generally pointed.
10. A mixing device as in claim 1 wherein the trailing edges of any
pair of said vanes are oriented with respect to the leading edges
of an adjacent pair of vanes such that a major portion of the
material transferred from said trailing edges initially contacts
said adjacent pair of vanes near said leading edges.
11. A mixing device as in claim 1 wherein the trailing edges of any
pair of said vanes are oriented with respect to the leading edges
of an adjacent pair of vanes such that a major portion of of
material transferred from said trailing edges initially contacts
said adjacent pair of vanes near the trailing edges of said
adjacent pair of vanes.
12. A mixing device as in claim 1 wherein said mixing elements are
unitarily connected, whereby said plurality of mixing elements may
be removed as a unit from said tube.
13. A mixing device as in claim 1 further including a plurality of
disks separating some of said plate-like members, said disks being
co-axial with the longitudinal axis of said tube and having at
least one aperture therethrough for relief of pressure, wherein
said vanes are angled from about 20.degree. to about 40.degree.
from the longitudinal centerline of said plate-like members, and
wherein the leading edge of said plate-like member is adapted for
slicing of solid material entering said tube.
Description
DETAILED DESCRIPTION
For a fuller understanding of the nature and objects of the
invention, reference is had to the following description taken in
conjunction with the accompanying drawings, in which:
FIG. 1 is an elevational view of a device of the invention with
some portions sectioned or shown diagrammatically;
FIG. 2 is a top, partially diagrammatic view of the device of FIG.
1;
FIG. 3 is an elevational, partly schematic view of one embodiment
of mixing element combination for use in a device of the
invention;
FIG. 4 is an elevational view of another embodiment of mixing
element combination;
FIG. 5 is an elevational view of still another embodiment of mixing
element combination of the invention;
FIG. 6 is a top view of a disk shown in the mixing element
combinations of FIGS. 4 and 5;
FIG. 7 is an elevational, partly schematic view of another
arrangement of the mixing element combination shown in FIG. 3;
FIGS. 8 and 9 are elevational, partly schematic views of two
embodiments of a portion of the mixing element illustrated in FIGS.
3, 4, 5 and 7; and
FIG. 10 is a side view of the mixing element portion of FIG. 9.
With reference to FIGS. 1-3, a motionless mixing device 21 of the
invention includes a hollow cylindrical tube 22 having an inlet and
outlet, preferably at opposite ends of the tube. For some
applications, as in countercurrent mixing, the inlet and outlet may
be in the same end of the tube or spaced closer together at some
point along the length of the tube. In the device of FIG. 1, the
inlet is covered by a cap member 23 and the outlet has a similar
capping member 24. Flow direction is from top to bottom, as
indicated by the arrow. The capping members may be provided with
suitable valving devices (not shown) and other elements for
connection with separate or converging inlet and outlet flow lines
(not shown). In the usual case, the capping elements are flanged
and have holes therethrough for bolting or for otherwise affixing
the mixing device to a suitable support or stage in a processing
operation. The details of such capping elements and other auxiliary
structure are well known and therefore require no further
description.
The primary mixing element 25 has three sections. The first is a
generally rectangular, flat, plate-like member 26. The other
sections are a pair of weirs or vanes 27 and 28 which are also flat
and plate-like in configuration but are not necessarily
rectangular. As shown, the vanes preferably have rounded edges and,
like the plate-like members 26, preferably are elongated in the
direction of the longitudinal axis of the tube 22. With respect to
the plate-like members 26, a length of about 1.4 times its width
has been found useful, but the relative dimensions may be varied as
desired. It will be noted that the longitudinal dimensions of the
vanes 27 and 28 are somewhat less than those of the plate-like
members 26 but these dimensions may generally correspond if
desired.
The vanes 27 and 28 are mounted perpendicularly on opposite faces
of the plate-like member 26 by any suitable means such as by
welding. The vanes are mounted such that their lateral axes are on
the centerlines of the plate-like member, and the vanes are angled
in opposite directions, as shown. Each vane preferably is angled
from about 20.degree. to about 40.degree. from the longitudinal
centerline of the plate-like member 26, best results being obtained
at an angle of about 30.degree.. A plurality of such mixing
elements 25 are stacked substantially end-to-end in the tube 22 so
that the angle between any adjacent plate-like members 26 is about
90.degree.. The mixing elements 25 are fixed within the tube 22
either individually as by welding or pinning through the wall of
tube 22 or, preferably, the mixing elements are welded or fastened
together to form a unitary string of elements. The plurality of
mixing elements when thus made unitary may be maintained clear of
the sides of the tube, their fixed position in relation to the tube
being determined by mounting contact with the capping members 23
and 24. Alternatively, in the preferred arrangement in which the
individual mixing elements 25 are unitarily fixed to each other,
each end of the completed assembly of mixing elements may be
pinned, welded or otherwise affixed to the inner walls or ends of
the tube 22, thus also providing a unitary combination of the tube
and mixing elements.
Clearances between the plate-like members 26, vanes 27 and 28, and
the inside wall of the tube 22 may be varied as desired for the
particular mixing operation. It will be evident that if the mixing
device is to be reused, a degree of clearance between the mixing
elements and the inside wall of the tube will be desirable, so that
the mixing device can be more easily cleaned.
The top end view of FIG. 2 illustrates the arrangement of
plate-like members 26 and vanes 27 and 28 relative to clearance and
channels of flow through the tube. As shown, the uppermost mixing
element has a plate-like member 26a and vanes 27a and 28a. Shown in
partially diagrammatic form below this uppermost element is the
next adjacent mixing element comprising a plate-like member 26b and
vanes 27b and 28b. It will be noted that the rounded edges of the
vanes provide a close fit within the tube but there is retained
four longitudinal channels which serve to avoid substantial
pressure drop as material moves through the tube, and to facilitate
cleaning.
In the embodiment of combination of mixing elements as shown in
FIG. 3, the relationship of the trailing edges 32 of one pair of
vanes 27 and 28 relative to the orientation of the leading edges 33
of the next adjacent pair of vanes 27 and 28 should be noted. In
this embodiment, which is especially useful for low and medium
viscosity mixtures, a major portion of the material moving
downwardly over the surfaces of vanes 27 and 28 meets the nearly
abutting leading edges 33 of the next pair of vanes with the result
that a new division of the material is achieved in a relatively
short space. As the material moves downwardly and off vanes 27 and
28, the flow of material is directed out towards the inside wall of
tube 22 but in opposite directions within the same cross sectional
region of the tube. As a result of the transverse currents, good
cross mixing is obtained, this result being efficiently promoted by
the relatively close spacing of adjacent pairs of vanes.
The transverse flow is promoted further by the placement of
disk-like members 29 between some of the mixing elements 25, such
as between each mixing element (FIG. 5) or between every other
mixing element 25 (FIG. 4). The transverse flow provided by the
disk 29 is sometimes called "plug flow" and is successful with
respect to the present mixing device, only if at least one aperture
31 is provided in the disk 29. The aperture 31 provides pressure
relief so that plugging or undue pressure drop do not occur at this
point. For certain applications, it may be desirable to provide
more than one of such holes 31. The disks 29 may vary in diameter
from about one-fourth to three-fourths of the inside diameter of
the tube 22, and preferably their diameter is about one-half of the
inside diameter of the tube 22.
For the mixing of high or moderately high viscosity materials, the
orientation of vanes 27 and 28 shown in FIG. 7 may be more
desirable. As compared with the arrangement of FIG. 3, the trailing
edges 32 of the vanes in FIG. 7 are positioned away from the
leading edges 33 of the next adjacent pair of vanes. The result is
a freer flow of material from one pair of vanes to the next since a
major portion of the material flowing from the trailing edges will
initially contact the adjacent pair of vanes near the trailing
edges of the latter pair of vanes rather than near their leading
edges. Accordingly, the flow of material through the tube will be
faster than in the arrangement of FIG. 3, given materials of the
same viscosity.
In mixing operations where good slicing or shearing action is
desirable, the leading edges of the mixing elements 25, especially
the leading edges of the plate-like members 26 but the leading
edges of the vanes as well if desired, may be curved, rounded or
otherwise adapted to promote this result. Whereas the embodiments
of the mixing elements shown in the preceding figures are rounded,
FIG. 8 shows a pointed plate-like member 35 with its angled or
otherwise pointed leading edge 36. A knife edge such as the knife
edge 37 on the plate-like member 38 illustrated in FIGS. 9 and 10
is another embodiment. The knife edge design is particularly
suitable for the efficient admixture of solid or semi-solid
materials.
In operation, materials to be mixed are admitted in one or more
streams to the inlet end of the tube 22 through the inlet cap 23,
either under fluid pressure or under gravity flow. Then begin
numerous divisions of the materials as they contact the leading
edges of the plate-like members 26 and the vanes 27 and 28. It
should be noted that the materials will divide almost
simultaneously into six paths, the first two divisions being to
each side of the plate-like member 26 and each of these divisions
then being further divided over the leading edges of the vanes 27
and 28. But division is not the only mixing means. The vanes 27 and
28, being angled in opposite directions, cause the divided material
to flow outwardly towards the inner walls of the tube 22, resulting
in good cross currents and cross mixing. As indicated, the division
is promoted by the slicing leading edges of the plate-like members
26 and/or vanes 27 and 28.
This essentially simultaneous, multiple division is a unique aspect
of the present invention and it will be noted that it is a function
of essentially a single mixing element, the combination of the
plate-like member 26 and the vanes 27 and 28. Accordingly, any
number of such mixing elements 25 may be combined and encased in
the mixing tube 22, and the diameter of the tube and its length may
be varied to satisfy the requirements of any mixing operation. For
example, tubes are commercially available having diameters of from
about three-sixteenths inch (inside diameter) to about 36 inches
(outside diameter), and lengths can range from a few inches to 30
feet and more.
Of course, diameters and lengths of tubes, as well as the
dimensions of the mixing elements, will depend on flow rates and
other empirically determined mixing requirements. The mixing device
of the invention can be designed from the data of simple
experiments and then scaled to suit any actual mixing requirement.
The device is useful for virtually unlimited combinations of
fluids, whether liquids or gases, as well as for combinations of
solids and fluids, or even for so-called "solid" mixtures.
Moreover, the mixing device may be easily manufactured from any
suitable material such as steel, metal alloys or heavy duty
plastics, and may be coated with various materials such as rubber
for use with highly corrosive or reactive materials.
The mixing device of the invention has all the advantages of known
motionless mixing devices with the additional advantages of low
cost construction, adaptability to almost any mixing operation, and
excellent aerating ability if such is desired. The relatively
simple elements of the device may be manufactured by simple
stamping techniques rather than by complex twist tooling, and the
pressure drops encountered within the device are comparable to
those of the best of the known motionless mixers for the same flow
rates and viscosities. Moreover, the numerous edges to which the
materials flowing through the tube are exposed, contributes to
"self-cleaning" qualities of the device, and sediments which
normally might cake in such a device, are carried through.
It will thus be seen that the objects set forth above, among those
made apparent from the preceding description, are efficiently
attained and, since certain changes may be made in the above
construction without departing from the spirit and scope of the
invention, it is intended that all matter contained in the above
description or shown in the accompanying drawings shall be
interpreted as illustrative and not in a limiting sense.
It is also to be understood that the following claims are intended
to cover all of the generic and specific features of the invention
herein described, and all statements of the scope of the invention
which, as a matter of language, might be said to fall
therebetween.
* * * * *