[0001] The invention concerns a mixing system designed to introduce chemical substances
in a fluid to be treated.
[0002] Nowadays clean water is considered a valuable resource which must be preserved and
used only in the cases where its consumption is absolutely necessary.
[0003] For example, the paper industry has always used huge quantities of fresh water, meaning
new water, in order to be able to obtain high quality products.
[0004] However, in the last few years environmental regulations and a greater environmental
awareness at a global level have been increasingly leading people to reduce water
consumption.
[0005] Today, for example, paper sludge is becoming increasingly important and is increasingly
used for producing other paper, in the tile and cement industry, in environmental
restoration projects, for covering dumps and in building mixes.
[0006] Some steps of a process for the treatment of the waste water of a paper mill include
the use of a polyelectrolyte, for example a cationic flocculant powder, or even, for
example, a cationic polyacrylamide, suited to be applied in the clariflocculation
of water containing organic substances, in sludge thickening treatments, in sludge
dehydration processes and also in other processes carried out in paper mills, such
as froth flotation.
[0007] During these process steps it is necessary to maximize the yield of the polymer,
that is, of the cationic flocculant, in order to improve the quality of the dry residue
in the case of sludge or to improve froth flotation in the case of a froth flotation
step.
[0008] In order to be activated, these polymers need premixing with water at a preestablished
concentration.
[0009] Nowadays, said premixing step is carried out in static mixing tanks, in which the
polymer is introduced after being taken from a small storage container; said polymers
are normally diluted in solutions between 0.2% and 1%, therefore they are very demanding
in terms of water usage.
[0010] In the static mixing tank mixing is obtained from the simple turbulence of water.
Successively, a booster pump introduces the water with the polymer into a pipe leading
to a tank or a channel for the treatment of waste sludge.
[0011] Thus, as already mentioned, these systems using a cationic flocculant, even if widely
used and appreciated, require the use of considerable quantities of water and of specific
mixing equipment, together with the corresponding ducts for preparation for use and
for introduction in a sludge treatment line.
[0012] Another limitation of the sludge treatment systems currently known lies in that the
polyelectrolytes are culture media for bacteria, therefore a polymer that remains
in a storage tank for long is very likely to foster the proliferation of bacteria.
[0013] The patent document
US5314076 describes a system for mixing two fluid phases, more specifically for mixing a treatment
fluid with a fluid to be treated; said system comprises two concentric chambers that
communicate with each other at least with their ends, the central chamber being provided
with two turbines whose rotation axis is equal to the axis of symmetry of the installation.
[0014] In this technical solution known in the art, the fluid to be treated flows in from
the top, flows out from the bottom and the turbines are interposed between the inlet
and the outlet.
[0015] The patent document
US2012/0199524 describes a clarifier silo comprising a closed container with an internal mixer surrounded
by a diffuser with a cylindrical tube.
[0016] The diffuser and the mixer define three internal chambers that are superimposed in
vertical direction, an upper chamber, a central chamber and a lower chamber, as well
as an external annular region. Each of the three internal chambers is in fluid communication
with the annular region.
[0017] Even in this technical solution known in the art, the fluid to be treated flows in
from the top, flows out from the bottom and the turbines are interposed between the
inlet and the outlet.
[0018] Even in the mixer described in patent document
US3392963, the fluid to be treated flows in from the top, flows out from the bottom and the
turbines are interposed between the inlet and the outlet.
[0019] The patent documents
US2577856 and
US3737288, instead, describe mixing equipment in which the fluid to be treated flows in from
the bottom and flows out from the top, and a propeller is interposed between the inlet
and the outlet.
[0020] The mixers and the equipment described in the above-mentioned patent documents are
not able to overcome the drawbacks and the limitations illustrated above.
[0021] It is the task of the present invention to provide a mixing system for the introduction
of chemical substances in a fluid to be treated, which can overcome the above-mentioned
drawbacks and limitations of the known art.
[0022] More specifically, it is an object of the invention to provide a mixing system that
makes it possible to drastically reduce the use of water for the preparation of a
polyelectrolyte suited to be introduced in the flow of waste fluid to be treated.
[0023] It is another object of the invention to provide a mixing system that favours the
reduction of energy consumption in waste water treatment processes.
[0024] It is a further object of the invention to provide a mixing system that improves
water retention from sludge, thus increasing the quantity of dry product obtainable
from sludge.
[0025] It is another object of the invention to provide a mixing system that can reduce
the waiting times for the beginning of the action of the polymer in solution on the
fluid to be treated, consequently improving the effectiveness of the polymer itself.
[0026] It is another object of the invention to provide a mixing system that is compact
and can be easily set up also in already existing waste water purification or treatment
plants or sludge drying plants.
[0027] It is another object of the invention to provide a mixing system that limits the
proliferation of bacteria on the same polyelectrolytes.
[0028] The task and the objects illustrated above are fulfilled by a mixing system for the
introduction of chemical substances in a fluid to be treated according to claim 1.
[0029] Further characteristics of the mixing system according to claim 1 are described in
the dependent claims.
[0030] The task and the objects illustrated above, together with the advantages described
below, are highlighted in the description of two embodiments of the invention, which
are provided by way of non-limiting example with reference to the attached drawings,
wherein:
- Figure 1 shows a schematic side sectional view of a first embodiment of a mixing system
according to the invention;
- Figure 2 shows a schematic side sectional view of a second embodiment of a mixing
system according to the invention.
[0031] With reference to Figure 1, in the context of a first embodiment, a mixing system
according to the invention is indicated by the numeral
10.
[0032] Said mixing system
10 comprises:
- a container 11 comprising an external wall 12, an internal wall 13, a bottom 14 and a cover 15,
- two concentric mixing chambers, a first central chamber 16 defined within the internal wall 13 and a second chamber 17 defined outside the internal wall 13, the first chamber 16 and the second chamber 17 being in communication with each other,
- an inlet duct 19 for a fluid to be treated, configured to introduce said fluid from the outside into
said first chamber 16,
- an outlet duct 20 for the treated fluid, said outlet duct 20 being configured to allow the outflow of said fluid from said second chamber 17 to the outside of said container 11,
said inlet duct
19, first chamber
16, second chamber
17 and outlet duct
20 being configured to define a labyrinthine mixing path
30,
- stirring blades 18 positioned inside the first chamber 16, operated by drive means through a rotation shaft 21,
- at least one injection passage 22 for the introduction of a chemical additive in one or more points of the labyrinthine
mixing path 30.
[0033] In the present example of embodiment, the second chamber
17 is to be understood as ring-shaped.
[0034] The labyrinthine mixing path
30 is indicated by arrows that schematically show the possible paths of the fluid being
treated between the inlet duct
19 and the outlet duct
20.
[0035] The drive means comprise, for example and not exclusively, a motor
35 configured to set the rotation shaft
21 rotating.
[0036] Said rotation shaft
21 carries the stirring blades
18.
[0037] The rotation axis of the rotation shaft
21 is parallel to the direction of extension of the internal wall
13.
[0038] More specifically, in the present non-limiting example of embodiment of the invention,
the external wall
12 has a cylindrical shape.
[0039] In the present non-limiting example of embodiment of the invention, also the internal
wall
13 has a cylindrical shape.
[0040] More specifically, the second chamber
17 surrounds the first chamber
16.
[0041] More specifically, the second chamber
17 is concentric and coaxial with the first chamber
16.
[0042] In said example of embodiment, the inlet duct
19 is positioned below the outlet duct
20 with respect to a configuration of use of the mixing system
10.
[0043] In said example of embodiment, the stirring blades
18 comprise a first group of blades
18a positioned at the lower end of the rotation shaft
21.
[0044] More specifically, said first group of blades
18a is positioned below the inlet duct
19 with respect to a configuration of use of the mixing system
10.
[0045] Said first group of blades
18a is to be understood as capable of being arranged also in another position along the
rotation shaft
21.
[0046] It is to be understood that the stirring blades
18 can be constituted by a single group of blades
18a.
[0047] In said example of embodiment, the stirring blades
18 comprise also a second group of blades
18b positioned in a central area of the rotation shaft
21.
[0048] More specifically, said second group of blades
18b is positioned above the inlet duct
19 with respect to a configuration of use of the mixing system
10.
[0049] The first chamber
16 and the second chamber
17 are in communication with each other through at least one passage opening
37 defined at the level of one end of the internal wall
13.
[0050] More specifically, but not exclusively, in said example of embodiment a first passage
opening
37 is defined by a lower recirculation space between a lower end
13a of the internal wall
13 and the bottom
14.
[0051] More specifically, but not exclusively, in said example of embodiment a second passage
opening
38 is defined by an upper recirculation space between an upper end
13b of the internal wall
13 and the cover
15.
[0052] In a variant embodiment, not illustrated for the sake of simplicity, the first chamber
16 and the second chamber
17 are in communication only through a lower passage opening
37; in said variant the upper end
13b of the internal wall
13 is in contact with the cover
15 and there is no upper passage opening
38.
[0053] In a further variant embodiment, not illustrated for the sake of simplicity, either,
the first chamber
16 and the second chamber
17 are in communication only through an upper passage opening
38; in said variant the lower end
13a of the internal wall
13 is in contact with the bottom
14 and there is no lower passage opening
37.
[0054] In said further variant embodiment, the inlet duct
19 and the outlet duct
20 are both advantageously positioned in proximity to the bottom
14 with respect to a configuration of use of the mixing system
10.
[0055] The mixing system
10 comprises a flow deviation element
40 configured to deviate the fluid flowing out of the first chamber
16 towards the second chamber
17.
[0056] Said flow deviation element
40 is placed on the bottom
14.
[0057] Said flow deviation element
40 is constituted by a body in the shape of a cone or truncated cone, configured to
deviate the flow towards the outside in radial direction, where the term 'radial'
is intended with respect to an axial direction of the axis of symmetry of the internal
wall
13, wherein the flow is flowing downwards from the first chamber
16.
[0058] The at least one injection passage
22 comprises a first injection pipe
22a directly connected to the inlet duct
19.
[0059] In a variant embodiment, said at least one injection passage
22 comprises, in addition or as an alternative, a second injection pipe
22b directly connected to the first chamber
16.
[0060] In a further variant embodiment, said at least one injection passage
22 comprises, in addition or as an alternative to one or both of the first injection
pipe
22a and second injection pipe
22b, a third injection pipe
22c directly connected to the second chamber
17.
[0061] A second embodiment of a mixing system is schematically represented in Figure 2 and
therein indicated by the numeral
110.
[0062] The specific characteristic of the mixing system
110 lies in that the container
111, comprising an external wall
112, an internal wall
113, a bottom
114 and a cover
115, comprises also an intermediate wall
150.
[0063] Said intermediate wall
150 defines, together with the external wall
112 and the internal wall
113, three concentric mixing chambers, a first central chamber
116 defined within the internal wall
113, a second intermediate chamber
117 that surrounds the first chamber
116 and a third external chamber
153 that surrounds the second chamber
117.
[0064] In said second embodiment of the mixing system
110 according to the invention:
- the first chamber 116 and the second chamber 117 are in communication with each other through at least one passage opening 137 defined at the level of one end of the internal wall 113, and at the same time
- the second chamber 117 and the third chamber 153 are in communication with each other through at least one passage opening 154 defined at the level of one end of the intermediate wall 150.
[0065] More specifically, but not exclusively, in said example of embodiment a first passage
opening
137 between the first chamber
116 and the second chamber
117 is defined by an upper recirculation space between an upper end
113a of the internal wall
113 and the cover
115.
[0066] More specifically, but not exclusively, in said example of embodiment a second passage
opening
138 between the first chamber
116 and the second chamber
117 is defined by a lower recirculation space between a lower end
113b of the internal wall
113 and the bottom
114.
[0067] More specifically, but not exclusively, in said example of embodiment a first passage
opening
154 between the second chamber
117 and the third chamber
153 is defined by a lower recirculation space between a lower end
150a of the intermediate wall
150 and the bottom
114.
[0068] More specifically, but not exclusively, in said example of embodiment a second passage
opening
155 between the second chamber
117 and the third chamber
153 is defined by an upper recirculation space between an upper end
150b of the intermediate wall
150 and the cover
115.
[0069] In a variant embodiment, not illustrated for the sake of simplicity, the first chamber
116 and the second chamber
117 are in communication only through an upper passage opening
137, and the second chamber
117 and the third chamber
153 are in communication only through a lower passage opening
154.
[0070] In a further variant embodiment, not illustrated for the sake of simplicity, either,
the first chamber
116 and the second chamber
117 are in communication only through a lower passage opening
138, and the second chamber
117 and the third chamber
153 are in communication only through an upper passage opening
155.
[0071] In said further variant embodiment, the inlet duct
119 and the outlet duct
120 are both advantageously positioned in proximity to the bottom
114 with respect to a configuration of use of the mixing system
110.
[0072] The mixing system
110 comprises a flow deviation element
140 configured to deviate the fluid flowing out of the first chamber
116 or the second chamber
117 towards the third chamber
153.
[0073] Said flow deviation element
140 is placed on the bottom
114.
[0074] Said flow deviation element
140 is constituted by a body in the shape of a cone or truncated cone, configured to
deviate the flow towards the outside in radial direction.
[0075] Analogously to what has been described above with reference to the first embodiment
of the invention, the mixing system
110 comprises an injection passage
122 for the introduction of a chemical additive in one or more points of the labyrinthine
mixing path
130.
[0076] According to its first embodiment illustrated in Figure 1, the mixing system
10 operates in such a way that the fluid to be treated, for example sludge, flows into
the first chamber
16 through the inlet duct
19 and, thanks to gravity and to the action of the stirring blades
18, flows downwards, towards the passage opening
37, in which it is deviated upwards into the second chamber
17; while flowing upwards along the second chamber
17 the treated fluid meets the outlet duct
20 and is conveyed into it.
[0077] A chemical additive, for example cationic polyacrylamide, is injected in the fluid
to be treated during its passage through said labyrinthine mixing path
30.
[0078] According to its second embodiment illustrated in Figure 2, the mixing system
110 operates in such a way that the fluid to be treated flows into the first chamber
116 through the inlet duct
119 and is conveyed upwards thanks to the action of the stirring blades
118.
[0079] Successively, the fluid follows a labyrinthine mixing path
130 in which it passes through all of the three chambers, the first
116, the second
117 and the third
153, and from the latter passes into the outlet duct
120.
[0080] It has practically been shown that the mixing system
10 and
110 according to the invention fulfils its task and achieves the set objects.
[0081] In fact, the invention provides a mixing system thanks to which the fluid to be treated
and the chemical additive are mixed with no need for the chemical additive to be prepared,
meaning diluted, in advance in costly and bulky water tanks, thus drastically reducing
water consumption.
[0082] The chemical additive, for example a cationic flocculant polymer, is activated when
it comes in direct contact with a fluid to be treated, and this happens directly inside
the first, the second and, if necessary, the third chamber.
[0083] Furthermore, the invention provides a mixing system which, thanks to the stirring
effect produced by the stirring blades, improves the effectiveness and the efficiency
of the chemical additive; for example, in the case of organic sludge, in which the
sludge has an apolar surface membrane, the strong stirring action favours the breakage
of said membrane and makes anionic sites available; the introduction of and the mixing
with a cationic polyelectrolyte make the anionic sites react with the cationic polyelectrolyte
releasing water molecules, which favours a greater separation of the solid fraction
of the fluid being treated from the liquid fraction.
[0084] Therefore, the invention provides a mixing system that makes it possible to drastically
reduce the use of water when preparing a polyelectrolyte intended to be introduced
in a flow of waste fluid to be treated.
[0085] In addition to the above, the invention provides a mixing system that favours the
reduction of energy consumption in waste water treatment processes, since it is no
more necessary to manage a mixing and storage tank and the efficiency in terms of
separation of the dry fraction from the liquid fraction is improved compared to the
known treatment systems.
[0086] In fact, the invention provides a mixing system that improves water retention from
sludge, thus increasing the quantity of dry product obtainable.
[0087] Moreover, the invention provides a mixing system that is capable of reducing waiting
times before the beginning of the action of the polymer in solution on the fluid to
be treated, consequently improving the effectiveness of the polymer itself; this has
been obtained by introducing the chemical additive directly in the fluid to be treated
and subjecting both of them to a mixing action produced by the stirring blades.
[0088] Furthermore, the invention provides a compact mixing system that can be easily set
up also in existing waste water purification or treatment systems or sludge drying
systems.
[0089] Furthermore, the invention provides a mixing system that limits the proliferation
of bacteria on the same polyelectrolytes, thanks to the direct introduction of the
same polyelectrolytes directly in the fluid to be treated, without providing for a
storage period before use.
[0090] The invention conceived in this way can be subjected to several modifications and
variants, all falling within the inventive concept disclosed herein; furthermore,
all the details can be replaced by other technically equivalent elements.
[0091] In practice, any components and any materials can be used, provided that they are
compatible with the intended use, and any shape and size can be selected, according
to the needs and the state of the art.
[0092] Where the characteristics and techniques mentioned in any of the claims are followed
by reference signs, it must be understood that these reference signs are used only
for the purpose of making the claims easier to understand, and consequently these
reference signs do not have any limiting effect on the interpretation of each element
identified by way of example by the same reference signs.
1. Mixing system (10) for the introduction of chemical substances in a fluid to be treated,
comprising:
- a container (11) comprising an external wall (12), an internal wall (13), a bottom
(14) and a cover (15),
- at least two concentric mixing chambers, a first central chamber (16) defined within
said internal wall (13) and a second chamber (17) defined outside said internal wall
(13), said first chamber (16) and second chamber (17) being in communication with
each other,
- an inlet duct (19) for a fluid to be treated, configured for the introduction of
said fluid from the outside into said first chamber (16),
- an outlet duct (20) for said treated fluid, configured for the outflow of said fluid
from said second chamber (17) to the outside of said container (11),
said inlet duct (19), first chamber (16), second chamber (17) and outlet duct (20)
being configured to define a labyrinthine mixing path (30),
- stirring blades (18) positioned inside said first chamber (16), operated by drive
means through a rotation shaft (21),
- at least one injection passage (22) for the introduction of a chemical additive
in one or more points of said labyrinthine mixing path (30),
characterized in that said inlet duct (19) is positioned below said outlet duct (20) with respect to a
configuration of use of said mixing system (10),
- said stirring blades (18) comprising at least one first group of blades (18a),
- said first group of blades (18a) being positioned below said inlet duct (19) with
respect to a configuration of use of the mixing system (10).
2. Mixing system according to claim 1, characterized in that said drive means comprise a motor (35) configured to set said rotation shaft (21)
rotating, wherein said rotation shaft (21) carries said stirring blades (18).
3. Mixing system according to one or more of the preceding claims, characterized in that said first chamber (16) and second chamber (17) are in communication with each other
through at least one passage opening (37) defined at the level of one end of said
internal wall (13).
4. Mixing system according to claim 3, characterized in that a first passage opening (37) is defined by a lower recirculation space between a
lower end (13a) of said internal wall (13) and said bottom (14).
5. Mixing system according to one or more of claims 3 and 4, characterized in that a second passage opening (38) is defined by an upper recirculation space between
an upper end (13b) of said internal wall (13) and said cover (15).
6. Mixing system according to one or more of the preceding claims, characterized in that it comprises a flow deviation element (40) configured to deviate said fluid flowing
out of said first chamber (16) towards said second chamber (17).
7. Mixing system according to one or more of the preceding claims, characterized in that said at least one injection passage (22) comprises an injection pipe (22a) directly
connected to said inlet duct (19).
8. Mixing system according to one or more of the preceding claims, characterized in that said at least one injection passage (22) comprises an injection pipe (22b) directly
connected to said first chamber (16).
9. Mixing system according to one or more of the preceding claims, characterized in that said at least one injection passage (22) comprises an injection pipe (22c) directly
connected to said second chamber (17).
10. Mixing system according to one or more of the preceding claims, characterized in that said container (111) comprising an external wall (112), an internal wall (113), a
bottom (114) and a cover (115) comprises also an intermediate wall (150), said intermediate
wall (150) defining, together with said external wall (112) and with said internal
wall (113), three concentric mixing chambers, a first central chamber (116) defined
within said internal wall (113), a second intermediate chamber (117) that surrounds
said first chamber (116) and a third external chamber (153) that surrounds said second
chamber (117).