U.S. patent number 3,581,886 [Application Number 04/839,367] was granted by the patent office on 1971-06-01 for two-stage electrostatic separation of particulate material.
This patent grant is currently assigned to Wintershall Aktiengesellschaft. Invention is credited to Heinz Erbe, Guenter Fricke, Arno Singewald.
United States Patent |
3,581,886 |
Singewald , et al. |
June 1, 1971 |
TWO-STAGE ELECTROSTATIC SEPARATION OF PARTICULATE MATERIAL
Abstract
Separation of potassium oxide containing salts into various size
fractions by passing a mass containing particulate and powder
fractions between two electrodes of an electrostatic precipitator;
maintaining the voltage across the electrodes such that the mass
separates into portions, that part adheres to the positive
electrode, part stays adjacent the positive electrode, part stays
adjacent the negative electrode, and part passes intermediate the
two electrodes; and recovering the individual parts separate from
each other.
Inventors: |
Singewald; Arno (Kassel-Wilh,
DT), Fricke; Guenter (Roeddense Ueber Lehrte,
DT), Erbe; Heinz (Diekholzen Ueber Hildesheim,
DT) |
Assignee: |
Wintershall Aktiengesellschaft
(Kassel, DT)
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Family
ID: |
26652310 |
Appl.
No.: |
04/839,367 |
Filed: |
July 7, 1969 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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592863 |
Nov 8, 1966 |
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Foreign Application Priority Data
Current U.S.
Class: |
209/9;
209/127.4 |
Current CPC
Class: |
B03C
7/00 (20130101) |
Current International
Class: |
B03C
7/00 (20060101); B03b 001/04 (); B03c 007/08 () |
Field of
Search: |
;209/127--131,9 |
References Cited
[Referenced By]
U.S. Patent Documents
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3217876 |
November 1965 |
Autenrieth |
3477566 |
November 1969 |
Autenrieth et al. |
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Foreign Patent Documents
Other References
Autenrieth, German Application 1154052 printed Sept. 12, 1963 (KL
156).
|
Primary Examiner: Lutter; Frank W.
Assistant Examiner: Halper; Robert
Parent Case Text
CROSS-REFERENCES TO RELATED APPLICATIONS
This is a continuation-in-part of our copending application, Ser.
No. 592,863 now abandoned, filed on Nov. 8,1966 under the title
"Method and Apparatus for Electrostatic Separation of Particulate
Material."
Claims
What we claim as new and desire to be secured by Letters Patent
is:
1. A process for the continuous electrostatic separation of ground
potassium raw salts containing finely divided particles and being
conditioned with a 10--15 percent aqueous solution of Na-salts of
straight-chain, lower fatty acids comprising the steps of (a)
establishing between successive areas of two endless traveling
surfaces of opposite polarity a first electrostatic field having a
strength of at least 3.5 and at most 4.5 kv./cm.; (b) feeding in a
predetermine direction through said electrostatic field a stream of
said potassium raw salts including particles having a grain size
smaller than 0.15 mm. and particles having a grain size larger than
0.15 mm. and containing a predetermined percentage range of K.sub.2
O whereby a dust concentrate consisting of particles having a grain
size up to about 0.15 mm. and containing between substantially
38--42 percent K.sub.2 O adheres to the positive one of said
electrodes, while a dust-free potassium oxide-rich preconcentrate
having a grain size greater than 0.15 mm. and containing 40--46
percent K.sub.2 O flows freely towards and past said positive
electrode, and a potassium-poor residue flows to the negative one
of said electrodes with a middling fraction passing intermediate
both of said electrodes; (c) brushing said dust concentrate off and
recovering it from said positive electrode; passing said middling
fraction through a second similar electrostatic field between two
additional electrodes of opposite polarity whereby an additional
dust-free preconcentrate containing K.sub.2 O and having a grain
size above about 0.15 mm. is separated from said middling fraction
and freely passes over the positive additional electrode, while a
residue poor in K.sub.2 O freely passes over the negative
additional electrode with a residual dust-free fraction passing
freely between both of said additional electrodes; and (d)
recirculating said residual middling fraction to said first
electrostatic field, together with new raw salts.
2. A process as defined in claim 1, wherein said stream is passed
through said fields in downward direction.
3. A process as defined in claim 1, wherein said raw salts are
hartsalz.
4. A process as defined in claim 1, wherein the step of brushing
said dust separately off said positive electrode comprises
subjecting said positive electrode to a brushing with a stationary
brush.
5. A process as defined in claim 1; and further comprising the
steps of separately subjecting said additional preconcentrate to
further separation into portions of higher and lower K.sub.2 O
concentration until a portion is obtained having a K.sub.2 O
concentration of between about 58 and 60 percent.
6. A process as defined in claim 1, wherein the steps of
establishing said electrostatic fields comprise establishing at
least said first electrostatic field at a field strength of between
substantially 4.0 and 4.5 kv./cm.
7. A process as defined in claim 6, wherein the steps of
establishing said electrostatic fields comprise establishing said
second electrostatic field also at a field strength of between
substantially 4.0 and 4.5 kv./cm.
8. A process for the continuous electrostatic separation, by means
of continuous electrode surfaces of an endless, conductive, moving
belt, of ground potassium raw salts containing finely divided
particles and being conditioned with a 10--15 percent aqueous
solution of sodium salts of straight chain, lower fatty acids,
comprising the steps of establishing between two electrodes of
opposite polarity in an electrostatic separator an electrostatic
field having a strength of at least 3.5 and at most 4.5 kv./cm.;
feeding in a predetermined direction through said electrostatic
field a stream of said potassium raw salts including particles
having a grain size smaller than 0.15 mm. and particles having a
grain size larger than 0.15 mm. and containing a predetermined
percentage range of K.sub.2 O, whereby a dust concentrate
consisting of particles having a grain size up to about 0.15 mm.
and containing between substantially 38--42 percent K.sub.2 O
adheres to the positive one of said electrodes, while a dust-free
potassium oxide-rich preconcentrate having a grain size greater
than 0.15 mm. and containing 40--46 percent K.sub.2 O flows freely
toward and past said positive electrode, and a potassium-poor
residue flows to the negative one of said electrodes with a
middling fraction passing intermediate both of said electrodes;
brushing said dust concentrate off and recovering it from said
positive electrode; and returning said middling fraction upstream
of said electrostatic field for renewed passage therethrough with
fresh raw salts.
9. A process as defined in claim 8, wherein the step of
establishing said electrostatic field comprises establishing said
field at a field strength of between substantially 4.0 and 4.5
kv./cm.
10. A process as defined in claim 9, wherein said stream is passed
through said field in downward direction.
11. A process as defined in claim 9, wherein said raw salts are
hartsalz.
12. A process as defined in claim 9; and further comprising the
step of subjecting said preconcentrate to further electrostatic
separation into portions of higher and lower K.sub.2 O
concentration until a portion is obtained having a K.sub.2 O
concentration of between about 58 and 60 percent.
Description
BACKGROUND OF THE INVENTION
The present invention relates to a method for the electrostatic
separation of particulate material and, more specifically, the
invention is concerned with a method for the electrostatic
treatment of crude potassium salts in particulate form and
including a fraction of very small, dustlike particles.
The separation of sylvite from dust-containing crude potassium
salts is connected with very considerable difficulties which it was
not possible up to now to overcome in a satisfactory manner. These
difficulties arise primarily due to the fact that the dustlike
fraction of the crude potassium salts will be unselectively charged
in an electrostatic field and, consequently, the dustlike particles
which will be collected together with the coarser particles of
higher potassium content and since these dustlike particles at
least partially have a relatively low potassium content, their
presence will reduce the K.sub.2 O concentration in the separated
particulate fraction of higher K.sub.2 O content. The dustlike
fraction is primarily selectively charged. It appears to be
unselectively charged because its constituent particles will
readily agglomerate, in which condition the selective charge
exchange is nullified with resultant adverse influencing of the
k.sub.2 O content of the concentrates and the residues. This occurs
particularly if the crude material includes dustlike fraction in a
quantity of 25 percent or more. If a crude salt is
electrostatically processed in accordance with the approach known
from the prior art and without prior separation of the dustlike
fraction, a large quantity of the dustlike fraction will enter the
concentration stage, together with the preconcentrate, and will be
returned from the concentration stage to the preconcentration stage
together with the middlings. This quantity of dustlike fraction,
that is the quantity contained in the middlings, will inevitably
cause the maximum permissible quantity of up to 25 percent in the
finished product to be exceeded.
Throughout the description and claims the potassium content will be
referred to as K.sub.2 O as an indication of the equivalent amount
of the potassium salts which are actually present.
A further difficulty in the concentration of sylvite from
dust-containing particulate crude potassium salts is caused by the
firm adherence of the dustlike particles at the electrodes of the
electrostatic separator, whereby again the electrostatic separation
of the coarser constituents of the particulate mass of crude
potassium salts into fractions of higher and lower K.sub.2 O
content will be impaired.
In view of the foregoing, it has been proposed to separate dustlike
particles from the particulate mass of crude potassium salts by
mechanical means such as screening, prior to the electrostatic
dressing of the particulate mass. However, such prescreening
requires a separate installation and is a relatively expensive
procedure and, furthermore, results in the separation of the
dustlike particles in a form in which same are substantially
without commercial value so that the thus separated mass of
dustlike particles has to be further processed, for instance
concentrated by dissolution in hot water followed by
crystallization.
The direct electrostatic separation of a mass consisting
essentially only of dustlike particles into fractions of higher and
lower K.sub.2 O content is not possible in a technically
satisfactory manner, due to the lack of selectivity of the dustlike
particles with respect to the acceptance of electrostatic charges
by the same.
By producing a concentrate in conventional manner, by electrostatic
separation which may be carried out as a single step or as a
two-step electrostatic separation, it is possible, for instance, to
separate hard salt into the following fractions:
However, such results are only intermittently obtained since upon
changes in the grain composition of the crude potassium salt,
particulately upon fluctuation in the proportion of dustlike
particles therein, the result is greatly impaired due to the fact
that unselectively separated dustlike particles continue to
circulate with the middlings throughout the process. Thus, in
actual industrial operation, for instance, separated fractions of
the following K.sub.2 O concentrations are obtained:
The above examples will serve to show that it is not possible by
using the above-described conventional processes to work in a
technically satisfactory manner with crude potassium salts which
contain a significant proportion of dustlike particles,
particularly hard salt.
SUMMARY OF THE INVENTION
It is therefore an object of the present invention to overcome the
above-discussed difficulties and disadvantages.
It is a further object of the present invention to provide a method
which will permit the working-up of crude potassium salts
containing a significant proportion of dustlike particles so as to
obtain a separated concentrated fraction of relatively high K.sub.2
O content and a residue of relatively very low K.sub.2 O
content.
It is a further object of the present invention to provide a method
for the electrostatic separation of dust-containing crude potassium
salts into fractions of higher and lower K.sub.2 O concentration
which can be carried out in a simple and particularly effective
manner.
Other objects and advantages of the present invention will become
apparent from a further reading of the description and of the
appended claims.
With the above and other objects in view, the present invention
contemplates a method of electrostatically separating a particulate
mass of crude potassium salts, including a dustlike fraction and
coarser particles of varying K.sub.2 O content, into the dustlike
fraction and into a plurality of fractions of progressively lower
K.sub.2 O concentration and substantially free of dustlike
particles, comprising the steps of passing a stream of the mass
through an electrostatic field formed between electrodes of
opposite polarity, the electrodes, respectively, exerting different
degrees of attraction with respect to the dustlike particles and
the coarser particles of higher and lower K.sub.2 O content of the
stream, so as to separate the mass into the dustlike fraction and
into a stream of coarser particles having a progressively lower
K.sub.2 O concentration in the direction from one of the electrodes
to the other, and separately recovering the dustlike fraction, and
the portions of the stream of highest, lowest and intermediate
K.sub.2 O concentration.
The present invention also provides in a device for the
electrostatic separation of particulate material into fractions of
particles having, respectively, different electrostatic
characteristics with respect to attraction of the same by
electrodes of opposite polarity, in combination, a pair of
elongated electrode means including electrodes of opposite
polarity, respectively, the electrode means being arranged spaced
from each other and forming between themselves a substantially
vertical path for the downward passage of a stream of particulate
material therethrough, at least one of the electrode means
including endless belt means rotating about the electrode of the
one electrode means and in part forming the path so that particles
which are strongly attracted by the one electrode will be caused to
adhere to the moving belt means, brush means operatively associated
with the moving belt means at a portion thereof spaced from the
path for separating adhering particles from the belt means, and
guide means located in the vicinity of the lower end of the path
for preventing contact between the downwardly passing stream and
the separated particles, and for recovering of the latter.
According to the present invention, it is possible to work up
dustlike particles-containing crude potassium salts in a manner
which permits separation of the dustlike fraction in the form of a
commercially valuable product containing about 40 percent K.sub.2
O.
Whereas according to the conventional methods of separating and
concentrating crude potassium salts in an electrostatic separator
three fractions are produced, namely a preconcentrate, middlings
and residue, the present invention provides for the additional
separation of a further concentrated fraction, namely a dustlike
fraction consisting of very small particles, generally having a
size of less than 0.15 mm. and containing about 40 percent K.sub.2
O.
This additional separation of the dustlike fraction having a
particle size of below about 0.1 or 1.15 mm. is carried out
simultaneously with the separation of the coarser particles of the
crude salt into preconcentrate, middlings and residue. Thereby the
further advantage is achieved that the separated fractions of
coarser particles will be substantially free of dustlike
particles.
Preferably, the method of the present invention is carried out in
an electrostatic separating device in which the crude salt
particles pass under the force of gravity downwardly through an
electrostatic field produced by two spaced electrodes which define
the path through which the stream of particulate potassium salt
moves in a downward direction. The crude potassium salt is
preferably preconditioned in conventional manner prior to being
introduced into the electrostatic separator, for instance by
treatment with straight-chain lower fatty acids. According to the
present invention, means are provided for dislodging dustlike
particles which under the force of the electrostatic field attach
themselves to an electrode, and for separately recovering the
thus-dislodged dustlike particles.
It has been found, surprisingly, that the dustlike fraction will
adhere to the electrodes at a certain specifically defined field
strength, while the coarser particulate fraction will freely travel
over the electrodes. This makes it possible to brush the adhering
dustlike fraction off the electrodes and to separate it from the
final product through the use of a separating trap which is
adjustable for particle separation.
Only after this was understood did it become possible to develop
the present approach to the processing in electrostatic separators,
particularly free-fall separators, of crude potassium salts
containing dustlike fraction. For example, to separate the dustlike
fraction below approximately 0.15 mm. grain size when raw salts are
conditioned with a 10--15 percent water solution of Na-salts of
fatty acids, a field strength of 3.5--4.5 kv./cm., preferably
4.0--4.5 kv./cm., is necessary.
The novel features which are considered as characteristic for the
invention are set forth in particular in the appended claims. The
invention itself, however, both as to its construction and its
method of operation, together with additional objects and
advantages thereof, will be best understood from the following
description of specific embodiments when read in connection with
the accompanying drawing.
BRIEF DESCRIPTION OF THE DRAWING
The single FIGURE is a schematic elevational view in the nature of
flow diagram, of a two-step electrostatic separation process
according to the present invention. 1 represents the dust
concentrate, 2 are the resultant middlings introduced into the
second separator, 3 the residue, 4 the coarse preconcentrate, 5 the
middlings from the second separator to be recycled, 6 represents
the endless belt electrode, and 7 the brush means.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
By proceeding in accordance with the present invention of
electrostatic separations it is possible, for instance, from a hard
salt containing 19.2 percent sylvite, 35.4 percent kieserite, 0.9
percent carnallite, 0.34 percent anhydrite, 1.64 percent insolubles
and 0.23 percent moisture, and having the following grain size
distribution: ##SPC1## ##SPC2##
It is thus possible to obtain from about 20 tons of the
above-described crude potassium salt in the first electrostatic
separation about 2 tons of a dustlike concentrate 1 of commercially
marketable quality. The dust-concentrate 1 may be sold and used as
such, for instance in the production of mixed or potassium
fertilizers, or it may be further worked up, in a manner known per
se, to form a granulated and commercially valuable product.
It will also be seen from the example given above that, by
proceeding in accordance with the present invention, it is possible
in the postseparation to further work up the concentrate 4 obtained
in the first separation, so as to arrive in the postseparation a
concentrate which has a K.sub.2 O content which is by 10 percent
higher than that which could be obtained without the separation of
dustlike particles in the prior art electrostatic separation
processes.
The possibility, according to the present invention, to obtain in a
simple and effective manner a commercial product having a K.sub.2 O
content of between 58 and 60 percent is of very great practical
significance.
Thus, the method of the present invention permits to obtain from a
crude potassium salt including dustlike particles between
two-thirds and three-fourths of the potassium, calculated as
K.sub.2 O in the form of a concentrated product containing between
58 and 60 percent K.sub.2 O, and between one-third and one-fourth
as a product containing between 38 and 40 percent K.sub.2 O.
It is also possible to utilize the dust concentrate 1 which is
obtained in the separation of hard salt and which contains between
38 and 40 percent K.sub.2 O and about 5 percent MgO for producing a
granulated magnesium-containing product which is commercially sold
under the designation "granulated potassium with MgO."
According to the invention, the dustlike particles 1 are separated
and withdrawn in the first electrostatic separation device. The
middlings 2 containing K.sub.2 O are introduced into a second
electrostatic separator wherein at the positive electrode a
practically dust-free concentrate 4 will be separated. The
middlings 5 of the second separation are preferably ground and then
recycled for reintroduction into the first electrostatic separating
device, together with additional preconditioned crude salt.
The residue 3 which accrues at the zones of the negative electrode
in the first and second separating device, is withdrawn in
conventional manner.
The process of the present invention thus provides for the
separation of a dust concentrate 1 from the fraction of coarser
salt particles 4.
By proceeding in this manner, and introducing 20 tons per hour of
crude salt into the illustrated electrostatic separator, it is
possible to recover 2 tons per hour of a dust concentrate 1
containing 40.5 percent K.sub.2 O and about 5 tons per hour of a
coarse preconcentrate 4 containing between 44 and 46 percent
K.sub.2 O. The dust concentrate 1 contains the dustlike particles
of sylvite having a size of less than 0.15 mm. and the coarse
concentrate 4 contains the coarser sylvite particles having a
particle size of 0.15--1.0 mm., which are then subjected to a
second electrostatic separation in order to obtain a product of up
to about 60 percent K.sub.2 O as described further above.
Without further analysis, the foregoing will so fully reveal the
gist of the present invention that others can, by applying current
knowledge, readily adapt it for various applications without
omitting features that, from the standpoint of prior art, fairly
constitute essential characteristics of the generic or specific
aspects of this invention and, therefore, such adaptations should
and are intended to be comprehended within the meaning and range of
equivalence of the following claims.
* * * * *