U.S. patent number 3,831,904 [Application Number 05/300,227] was granted by the patent office on 1974-08-27 for common plane sequential mixing apparatus.
This patent grant is currently assigned to Akzona Incorporated. Invention is credited to Jacques W. J. Appeldoorn, Robert Sluijters.
United States Patent |
3,831,904 |
Appeldoorn , et al. |
August 27, 1974 |
COMMON PLANE SEQUENTIAL MIXING APPARATUS
Abstract
An improved mixer with no moving parts is obtained by arranging
mixing elements in side-by-side relationship.
Inventors: |
Appeldoorn; Jacques W. J.
(Arnhem, NL), Sluijters; Robert (Arnhem,
NL) |
Assignee: |
Akzona Incorporated (Erka,
NC)
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Family
ID: |
27351529 |
Appl.
No.: |
05/300,227 |
Filed: |
October 24, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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83402 |
Oct 23, 1970 |
3701619 |
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Foreign Application Priority Data
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Nov 14, 1969 [NL] |
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6917131 |
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Current U.S.
Class: |
366/337;
138/38 |
Current CPC
Class: |
B01F
5/0604 (20130101); D01D 1/065 (20130101) |
Current International
Class: |
D01D
1/06 (20060101); D01D 1/00 (20060101); B01F
5/06 (20060101); D01d 003/00 () |
Field of
Search: |
;425/131,464,198,DIG.49,207 ;259/4 ;264/171 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Baldwin; Robert D.
Attorney, Agent or Firm: Craig & Antonelli
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATION
This application is a divisional of U.S. application Ser. No.
83,402 filed Oct. 23, 1970 and now U.S. Pat. No. 3,701,619.
Claims
We claim:
1. An apparatus, having no moving parts, for mixing or homogenizing
one of more viscous liquids comprising:
a. a first body having two substantially parallel end faces, said
first body containing a plurality of mixing elements with inlets
and outlets arranged adjacent to each other in a common plane, the
inlets and outlets of adjacent mixing elements being located in the
same face, said mixing elements having two or more substantially
axial flow ducts, each of which converges and diverges to divide
the viscous liquids into layers;
b. a second body operatively engaging one end face of the first
body and having therein a passage for receiving and directing one
or more viscous liquids to the inlet of an initial mixing element,
and channels for connecting the inlets and outlets of adjacent
mixing elements in the end face in a pattern; and
c. a third body operatively engaging the other end face of the
first body and having therein channels for connecting the inlets
and outlets of adjacent mixing elements in the other end face in a
pattern, and a passage for discharging the viscous liquids from the
exit of a final mixing element, the pattern of the channels being
such as to guide the viscous liquids sequentially through each of
the mixing elements to repeatedly divide and double the liquids to
provide intensive mixing.
2. The apparatus of claim 1, wherein the number of mixing elements
is not more than 30.
3. The apparatus of claim 1, wherein the number of mixing elements
is between 15 and 25.
4. The apparatus of claim 1, wherein two first bodies of identical
construction are mated adjacent each other between said second and
third bodies, said two first bodies being turned 180.degree.
relative to each other in such a manner that the outlet of a mixing
element and one first body is directly aligned with the inlet of a
mixing element in the other first body, the combination of the two
first bodies cooperating with said second and third bodies to
provide intensive mixing of the liquids.
5. An apparatus for mixing or homogenizing one or more high-viscous
liquids comprising:
a. a body having two end faces, said body containing a plurality of
mixing elements, each mixing element having inlets and outlets
adjacent to each other in a common plane of said body with the
inlets and outlets of adjacent mixing elements being located in the
same end face of said body, said mixing elements each having means
for dividing a viscous liquid flowing axially therethrough into
layers;
b. a first flow directing means operatively associated with the one
end face of said body, said first flow directing means including
passage means for supplying a viscous liquid to the inlet of one of
said plurality of mixing elements and for interconnecting the
inlets and outlets of adjacent mixing elements on said one end
face; and
c. a second flow directing means operatively associated with the
other end face of said body, said second flow directing means
including passage means for discharging a viscous liquid from a
mixing element other than said one mixing element and for
interconnecting the inlets and outlets of adjacent mixing elements
on said other end face, the passage means of said first and said
second flow directing means being so arranged that the viscous
liquid supplied to one mixing element successively flows through
each of said mixing elements until the liquid is discharged from
said other element whereby said liquid is repeatedly divided into
layers to provide intensive mixing thereof prior to discharge from
said other element.
6. The apparatus of claim 5, wherein the means for dividing a
viscous liquid flowing axially through said element into layers
comprises two or more substantially axial flow ducts, each of said
ducts converging and diverging to divide said viscous liquid into
layers.
7. The apparatus of claim 5, wherein the central axis of each of
said plurality of mixing elements is parallel to the other mixing
elements.
8. The apparatus of claim 5, wherein the passage means of said
first and second flow-directing means are so arranged that the
viscous liquid is successively passed in opposite directions
through said plurality of mixing elements.
9. The apparatus of claim 5, wherein the length of each of said
mixing elements has a minimum height corresponding to the thickness
of said body.
10. An apparatus for mixing a viscous liquid, comprising:
a. an assembly housing;
b. a first body mounted in the assembly housing and having two
substantially parallel end faces, said first body containing a
plurality of mixing elements having inlets and outlets adjacent to
each other in a common plane with the inlets and outlets of
adjacent mixing elements being located in the same end face of said
body, said mixing elements having means for dividing a viscous
liquid flowing axially through said elements into layers;
c. a second body mounted in said assembly above and in contact with
one end face of said first body, said second body having passage
means for receiving a viscous liquid and for directing the liquid
to the inlet of one of said mixing elements and additional passage
means for interconnecting the inlets and outlets of the adjacent
mixing elements in said one end face of said first body in a
pattern; and
d. a third body mounted in the assembly housing below and in
contact with the other end face of said first body, said third body
having passage means for interconnecting the inlets and outlets of
adjacent mixing elements in the other end face of said first body
in a pattern and additional passage means for directing viscous
liquid from the outlet of a mixing element other than said one
mixing element to an outlet of said housing, the patterns of the
passage means in said second and third bodies being such that the
viscous liquid is sequentially guided through each of the mixing
elements to repeatedly divide and double the number of layers of
liquid therein prior to discharge from said housing.
Description
This invention relates to a new use of the apparatus previously
disclosed in U.S. Pat. Nos. 3,051,453 and 3,182,965. More
particularly, this invention relates to apparatus for mixing or
homogenizing one or more high-viscous liquids to effect heat
transfer, cause a reaction, or divide the liquids into parallel
layers.
An object of this invention is the combination of apparatus for
mixing or homogenizing one or more liquids in an assemblage for
melt spinning of synthetic yarn. Another object of this invention
is to provide apparatus for mixing or homogenizing one or more
liquids in a minimum height. Still another object of this invention
is to provide apparatus of a minimum height for mixing or
homogenizing one or more liquids in an assemblage for melt spinning
synthetic yarn. Another object of this invention is to provide
apparatus for use as a heat exchanger or as a reactor for carrying
out chemical reactions.
A number of apparatus utilizing motionless blenders for imparting a
close degree of blending to high viscous fluids are known,
including those described in the above-mentioned patents. A common
characteristic of these apparatus is the in-line combination of
flow-diverting elements requiring a high length-to-width ratio of
the combined elements. Certain processes, such as melt spinning of
synthetic yarns, may extend for a height of several floors in a
plant building. In such processes it is desirable to minimize the
height requirements of each process step. It is also desirable when
melt spinning synthetic yarn to have a high degree of homegeneity
of the liquid polymer prior to spinning. It is evident the known
apparatus, while adequate, would add substantially to the overall
height of such a process. The present invention discloses a method
of maintaining the close degree of controlled mixing of known
apparatus in a minimum height.
The apparatus of the present invention comprises a multiplicity of
mixing elements or liquid-guiding members as described in the
above-mentioned patents in a given arrangement on the same plane,
the central axis of each mixing element being parallel to other
mixing elements. Interconnecting channels between outlets and
inlets of the mixing elements permit sequential mixing in a minimum
of height. One or more liquids from a given supply source is
directed through a mixing element of the type with two or more
substantially axial-flow channels, each of which successively
converges and diverges. The resultant liquid is directed to an
adjacent element inlet by an interconnecting channel.
A preferred embodiment of the apparatus according to the invention
has only the first mixing element connected to a supply channel for
receiving liquid and only the last mixing element connected to a
liquid discharge channel. The mixing elements may be cast in a
disc-shaped body. Interconnecting channels between the mixing
elements may be located in adjacent discs contiguous to the central
disc-shaped body.
According to the invention the number of mixing elements may be
even or odd. Two or more discs may be mounted adjacent each other
in such a manner that the outlet of a mixing element in the first
disc is directly aligned with the inlet of a mixing element of the
second disc.
The apparatus according to the invention permits the application of
a large number of mixing elements in a minimum height,
corresponding to the thickness of the disc. The number of guiding
members will generally not be more than 30 and preferably between
15 and 25.
BRIEF DESCRIPTION OF THE DRAWINGS:
FIG. 1 shows a disc with mixing elements in plan view;
FIG. 2 is a cross-sectional view of the disc of FIG. 1, installed
in a spinning assembly;
FIG. 3 is a plan view of two discs with mixing elements, one disc
on top of the other;
FIG. 4 is a cross-sectional view of the discs of FIG. 3, installed
in a spinneret assembly; and
FIGS. 5 and 6 represent block diagrams of discs with different
groups of mixing elements.
In FIG. 1, there are nineteen mixing elements that are arranged
side by side in the plane of disc 1 and at some distance from one
another, the mixing elements generally being referred to by numeral
2. The mixing elements 2 each comprise two axial flow ducts, each
of which successively converges and diverges in a plane turned
through an angle of 90.degree., as described in U.S. Pat. No.
3,051,453. The longitudinal axis of each mixing element is
perpendicular to the end faces 3 of disc 1. As can be seen from
FIG. 2, disc 1 is installed between two other disc-shaped bodies 5
and 6 in a housing 4 of a partially shown melt spinning assembly.
FIG. 2 shows discs 1, 5 and 6 in a cross section along Line II--II
of FIG. 1. In FIG. 1, the nineteen mixing elements 2 are numbered
from 101 through 119 to indicate the sequence of flow. One or more
molten polymers are supplied from above disc 5 to first mixing
element 101. From the exit of 101 the liquid stream flows via a
connecting channel in disc 6 to the inlet of mixing element 102.
From the exit of 102 the liquid stream flows via another connecting
channel in disc 5 to the inlet of mixing element 103. In this way
the liquid successively passes through all the mixing elements 101
to 119. In FIG. 2 a cross-sectional view is shown of mixing
elements 106, 109, 110, 111, and 114 and connecting channels 7, 8,
13, 14 and 15. Interconnecting channel 13, for example, connects
mixing elements 106 and 107 as shown by flow arrows in FIG. 1. The
stream of liquid passes in a downward direction through the last
mixing element 119 to orient it through channel 9, shown by a
broken line, into chamber 10 positioned over a spinneret plate 11.
The spinneret plate contains a large number of orifices 12 shown by
vertical lines.
Disc 1 may be cast in one piece from stainless steel by the lost
wax casting process. The mixer obtained is compact and has a very
intensive mixing action. Two unmixed liquid components supplied to
the first mixing element are divided into two layers upon passage
through that first mixing element. Through each successive mixing
element the components are repeatedly divided and doubled so that,
at the end of the nineteenth member, the number of layers of the
two components is 2.sup.19, indicating a very intensive mixing of
the two initially unmixed streams.
A slightly different embodiment is shown in FIGS. 3 and 4. Two
discs of identical construction are turned 180.degree. relative to
each other about their central axis in housing 4 of a spinning
assembly. In each disc there are nine mixing elements 201 through
209.
FIGS. 5 and 6 are schemes for the application of mixing elements in
groups of 15 and 25. At the top and bottom sides of the discs the
connecting channels between successive mixing elements are shown by
full and broken lines respectively. The scheme according to FIG. 5
is particularly suitable for application in melt spinning
assemblies comprising a rectangular spinneret plate.
* * * * *