Background of the Invention
[0001] The present invention relates to an air-gas mixing unit with an air-gas mixer which
comprises a main flow passage for mixing a first fluid with a second fluid into a
mixed fluid, the main flow passage comprising an inlet end for inlet of the first
fluid, at least one lateral inlet opening for inlet of the second fluid, and an outlet
end for outlet of the mixed fluid.
[0002] From the state of the art, an air-gas mixing unit with an air-gas mixer which comprises
a main flow passage for mixing a first fluid with a second fluid into a mixed fluid
is known. The main flow passage comprises an inlet end for inlet of the first fluid,
at least one lateral inlet opening for inlet of the second fluid, and an outlet end
for outlet of the mixed fluid. The air-gas mixer may e.g. be a Venturi-type mixing
nozzle that mixes air that forms the first fluid, with gas, such as hydrocarbon gas
or hydrogen gas, that forms the second fluid, into a combustible air-gas mixture that
forms the mixed fluid, with a desired concentration or ratio.
[0003] The document
EP 3 919 815 A1 describes such a Venturi-type mixing nozzle that is intended for mixing of air and
hydrogen gas. This Venturi-type mixing nozzle further comprises at least one bluff
body that is arranged in the main flow passage such that its wake shields the at least
one lateral inlet opening.
Summary of the Invention
[0004] The present invention relates to an air-gas mixing unit comprising an air-gas mixer
and a bluff body plate, wherein the air-gas mixer comprises a main flow passage for
mixing a first fluid with a second fluid into a mixed fluid. The main flow passage
comprises an inlet end for inlet of the first fluid, at least one lateral inlet opening
for inlet of the second fluid, and an outlet end for outlet of the mixed fluid. The
bluff body plate comprises at least one first bluff body arrangement with at least
one first bluff body, and at least one second bluff body arrangement with at least
one second bluff body, the at least one first bluff body being adapted to enable creation
of low pressure with a first degree of turbulence of the first fluid in the main flow
passage around the at least one lateral inlet opening, and the at least one second
bluff body being adapted to enable creation of low pressure with a second degree of
turbulence of the first fluid in the main flow passage around the at least one lateral
inlet opening.
[0005] Advantageously, the at least one first or second bluff body is positioned in the
main flow passage upstream of the at least one lateral inlet opening such that its
wake shields the at least one lateral inlet opening. The pressure in the shielded
region of the at least one lateral inlet opening may, thus, be reduced compared to
the pressure in circumjacent unshielded regions of the passage constriction, such
that pressure loss at the at least one lateral inlet opening is significantly reduced.
As a result, injection of the second fluid into the main flow passage and, thus, mixing
of the first and second fluids is improved and performed over a significantly reduced
longitudinal length inside of the air-gas mixer. Moreover, a required supply pressure
for the second fluid may advantageously be reduced.
[0006] Furthermore, provision of the bluff body plate with the at least one first bluff
body arrangement and the at least one second bluff body arrangement allows to convert
the inventive air-gas mixing unit easily, quickly and reliably from use with a first
type of gas, such as a hydrocarbon gas, e.g. methane, to a second type of gas, such
as hydrogen gas. More specifically, this may advantageously be achieved by merely
switching the air-gas mixing unit and, more particularly, the air-gas mixer from use
of the at least one first bluff body arrangement to use of the at least one second
bluff body arrangement.
[0007] According to one aspect, the bluff body plate is exchangeable to enable provision
of different bluff body arrangements which are configured for use with different types
of gases, wherein the different bluff body arrangements comprise different properties
of optimizing mixing and pressure losses.
[0008] Thus, different bluff body arrangements may be provided for a given type of gas to
optimize mixing and pressure losses in the air-gas mixer.
[0009] According to one aspect, the bluff body plate is re-orientable relative to the air-gas
mixer to enable positioning of the at least one first bluff body arrangement or the
at least one second bluff body arrangement at the inlet end of the air-gas mixer.
[0010] Thus, the inventive air-gas mixing unit may easily, quickly and reliably be switched
from use with a first type of gas, such as a hydrocarbon gas, e.g. methane, to a second
type of gas, such as hydrogen gas, by merely re-orienting the bluff body plate relative
to the air-gas mixer.
[0011] Preferably, the bluff body plate is rotatable or flippable between a first position
and a second position relative to the air-gas mixer, wherein the at least one first
bluff body arrangement is positioned at the inlet end of the air-gas mixer in the
first position, and wherein the at least one second bluff body arrangement is positioned
at the inlet end of the air-gas mixer in the second position.
[0012] Thus, a required re-orientation of the bluff body plate relative to the air-gas mixer
may easily and reliably be achieved.
[0013] According to one aspect, at least one of the at least one first bluff body arrangement
and the at least one second bluff body arrangement defines a throat of the air-gas
mixer at the inlet end.
[0014] Thus, a required throat of the air-gas mixer may advantageously be embodied by means
of the at least one first bluff body arrangement or the at least one second bluff
body arrangement.
[0015] According to one aspect, the air-gas mixer comprises a plurality of lateral inlet
openings, wherein at least one of the at least one first bluff body arrangement and
the at least one second bluff body arrangement is configured to impede at least one
of the plurality of lateral inlet openings.
[0016] Accordingly, a required air-gas ratio may securely and reliably be adjusted.
[0017] Preferably, the at least one of the at least one first bluff body arrangement and
the at least one second bluff body arrangement that is configured to impede the at
least one of the plurality of lateral inlet openings is embodied to enable a high
velocity flow of the first fluid at the at least one of the at least one first bluff
body arrangement and the at least one second bluff body arrangement.
[0018] By enabling a high velocity flow of the first fluid at the at least one of the at
least one first bluff body arrangement and the at least one second bluff body arrangement,
the at least one of the plurality of lateral inlet openings may easily be impeded.
[0019] According to one aspect, the at least one first bluff body of the at least one first
bluff body arrangement and the at least one second bluff body of the at least one
second bluff body arrangement are attached to, or integrally formed with, the bluff
body plate.
[0020] Accordingly, a robust and solid bluff body plate may be provided.
[0021] According to one aspect, the at least one first bluff body arrangement comprises
a plurality of first bluff bodies with differing shapes.
[0022] Thus, creation of a low pressure with a first degree of turbulence of the first fluid
in the main flow passage around the at least one lateral inlet opening may easily
be improved, thereby further improving mixing of the first and second fluids.
[0023] According to one aspect, the air-gas mixer is a Venturi-type mixing nozzle with a
nozzle body that forms the main flow passage.
[0024] Thus, a well-known type of mixing nozzle may advantageously be used to embody the
air-gas mixer.
Brief Description of the Drawings
[0025] Exemplary embodiments of the present invention are described in detail hereinafter
with reference to the attached drawings. In these attached drawings, identical or
identically functioning components and elements are labelled with identical reference
signs and they are generally only described once in the following description.
- Fig. 1
- shows a perspective view of a Venturi-type mixing nozzle with bluff bodies,
- Fig. 2
- shows a sectional view of the Venturi-type mixing nozzle of Fig. 1,
- Fig. 3
- shows a schematic view of exemplary flows of first and second fluids in the Venturi-type
mixing nozzle of Fig. 1 and Fig. 2,
- Fig. 4
- shows a perspective view of a Venturi-type mixing nozzle with bluff bodies according
to a variant, for an air-gas mixing unit according to the present invention,
- Fig. 5
- shows a top view of an air-gas mixing unit according to a first embodiment,
- Fig. 6
- shows a top view of an air-gas mixing unit according to a second embodiment,
- Fig. 7 to Fig. 9
- show sectional views of alternative air-gas mixing units, and
- Fig. 10
- shows a schematic view of an air-gas mixer with an alternative bluff body arrangement.
Detailed Description
[0026] Fig. 1 shows an illustrative Venturi-type mixing nozzle 100 with a nozzle body 105
that forms a main flow passage 110. The Venturi-type mixing nozzle 100 as such is
shown as one example of an air-gas mixer that may be used in an air-gas mixing unit
according to the present invention. More specifically, the Venturi-type mixing nozzle
100 may used for mixing of a combustible gas, e.g. hydrogen gas or a hydrocarbon gas,
such as methane, with air at a desired concentration or ratio in an associated air-gas
mixing unit that embodies a combustion device. Such a combustion device may e.g. be
used in building heating systems.
[0027] The main flow passage 110 has an inlet end 120 with a throat 199, and an outlet end
130 and is illustratively formed along the longitudinal direction of the nozzle body
105. More specifically, the main flow passage 110 in the nozzle body 105 is generally
formed as a tubular channel with a smooth inner surface.
[0028] Illustratively, the main flow passage 110 has a passage constriction 140 that is
arranged between the inlet end 120 and the outlet end 130. The passage constriction
140 represents the region with the smallest diameter of the throat 199.
[0029] By way of example, the main flow passage 110 is funnel-shaped between the inlet end
120 and the passage constriction 140 and, thus, having a converging inflow section.
Between the passage constriction 140 and the outlet end 130, the main flow passage
110 is illustratively conical and, thus, having a diverging outflow section.
[0030] By way of example, at least one bluff body is arranged in the main flow passage 110
between the inlet end 120 and the passage constriction 140, i.e. in the converging
inflow section. Illustratively, a plurality of bluff bodies 150 is provided but, however,
only a single bluff body is separately labelled with the reference sign 151, for simplicity
and clarity of the drawing. In the following description, reference is generally made
to the bluff body 151, representative for all respectively provided bluff bodies of
the plurality of bluff bodies 150.
[0031] The bluff body 151 protrudes preferably from the smooth inner surface of the main
flow passage 110 and is - in the illustrated example - attached to, or integrally
formed with, the nozzle body 105. In other words, the bluff body 151 is formed as
a bump or dent on the otherwise smooth inner surface inside of the main flow passage
110 and, thereby, forms an additional constriction of the main flow passage 110.
[0032] However, it should be noted that the bluff body 151 is only illustratively attached
to, or integrally formed with the nozzle body 105 to simplify description of an illustrative
operation of the Venturi-type mixing nozzle 100 with the bluff body 151 at Fig. 2
and Fig. 3 below. Nevertheless, according to the present invention the bluff body
151 is preferably embodied separate from the nozzle body 105, as described by way
of example at Fig. 4 below, and preferentially integrated into a bluff body plate
(505 or 605 in Fig. 5 to Fig. 9), as described by way of example at Fig. 5 to Fig.
9 below.
[0033] Fig. 2 shows the Venturi-type mixing nozzle 100 of Fig. 1 with the nozzle body 105
that forms exemplarily along its nozzle body central axis 290 the main flow passage
110 having the inlet end 120, the outlet end 130, and the passage constriction 140.
Illustratively, the nozzle body central axis 290 is a plane of symmetry.
[0034] The passage constriction 140 is arranged between the inlet end 120 and the outlet
end 130 for creation of a negative pressure region 125 in the main flow passage 110
during operation of the Venturi-type mixing nozzle 100. The negative pressure region
125 is only by way of example and for illustration purposes delimited by means of
two dashed lines.
[0035] Preferably, the passage constriction 140 comprises at least one lateral inlet opening.
By way of example, a plurality of lateral inlet openings is provided but, however,
only two lateral inlet openings are illustrated and separately labelled with the reference
signs 220, 221, for simplicity and clarity of the drawing. In the following description,
reference is generally made to one or both of the lateral inlet openings 220, 221,
representative for all respectively provided lateral inlet openings.
[0036] As described above at Fig. 1, the bluff body 151 is preferably arranged in the main
flow passage 110 between the inlet end 120 and the passage constriction 140. More
specifically, the bluff body 151 is preferably arranged in the main flow passage 110
between the inlet end 120 and the lateral inlet opening 221.
[0037] By way of example, one bluff body is provided for each lateral inlet opening. However,
at least one bluff body may alternatively also be provided for two or more lateral
inlet openings. In other words, it is possible to provide even only a single bluff
body for all lateral inlet openings.
[0038] The bluff body 151 preferably extends at least partly from the nozzle body 105 and,
more particularly, from the smooth inner surface of the main flow passage 110 towards
the nozzle body central axis 290, preferentially in radial direction 107 of the main
flow passage 110, for creation of an associated low pressure zone during operation
of the Venturi-type mixing nozzle 100. A respective low pressure zone that is associated
with the bluff body 151 is illustratively labelled with the reference sign 241 and
another low pressure zone is illustratively labelled with the reference sign 240.
Each one of the low pressure zones 240, 241 preferably extends from its associated
lateral inlet opening 220, 221 along the respectively associated bluff body, preferentially
in the radial direction 107 of the main flow passage 110.
[0039] In an illustrative operation of the Venturi-type mixing nozzle 100, a first fluid
210 enters the main flow passage 110 via the inlet end 120 and a second fluid 230
enters the main flow passage 110 via the lateral inlet openings 220, 221 for being
mixed with the first fluid 210 in the main flow passage 110 into a mixed fluid 235.
By way of example, the first fluid 210 is air and the second fluid 230 is a combustible
gas, e.g. hydrogen gas or a hydrocarbon gas, such as methane. More specifically, the
first fluid 210 that enters the main flow passage 110 via the inlet end 120 backs
up in the converging section between the inlet end 120 and the passage constriction
140 such that the negative pressure region 125 is created due to an acceleration of
the first fluid 210 by means of the nozzle effect. Since the lateral inlet openings
220, 221 open into the passage constriction 140, the second fluid 230 is drawn into
the main flow passage 110, where the second fluid 230 is mixed with the first fluid
210 into the mixed fluid 235. Illustratively, the second fluid 230 is guided to the
lateral inlet openings 220, 221 via associated support channels 227, 229, which are
illustratively arranged at an angle of 90° relative to the nozzle body central axis
290.
[0040] By way of example, the bluff body 151 is provided for creation of the low pressure
zone 241 in the negative pressure region 125 such that the first fluid 210 has a flow
velocity in the low pressure zone 241 that is at least reduced compared to a flow
velocity that is otherwise attributed to the first fluid 210 in the negative pressure
region 125. More particularly, the bluff body 151 is preferably adapted to ensure
that the second fluid 230 is fully surrounded by the first fluid 210 after having
entered the main flow passage 110 through the lateral inlet opening 221.
[0041] Fig. 3 shows a section of the main flow passage 110 with the throat 199 that is formed
by the nozzle body 105 of the Venturi-type mixing nozzle 100 of Fig. 1 and Fig. 2.
Illustratively, the bluff body 151 protrudes from the smooth inner surface of the
main flow passage 110 at a predetermined position upstream of the lateral inlet opening
220. The bluff body 151 is preferably attached to, or integrally formed with, the
nozzle body 105.
[0042] Illustratively, the bluff body 151 creates at least partly turbulences of the first
fluid 210 flowing around the bluff body 151 and, more particularly, a low pressure
with a first degree of turbulences 310 of the first fluid 210. Preferably, the low
pressure with the first degree of turbulences 310 of the first fluid 210 is at least
created in the negative pressure region 125.
[0043] In an illustrative operation of the Venturi-type mixing nozzle 100, the second fluid
230 is drawn through the lateral inlet opening 220 along the bluff body 151 into the
main flow passage 110 such that the first fluid 210 flows along the throat 199 and
directly surrounds the second fluid 230 downstream of the lateral inlet opening 220.
By creating the low pressure with the first degree of turbulences 310 of the first
fluid 210 around the second fluid 230, mixing of the first and second fluids 210,
230 is improved.
[0044] Fig. 4 shows a Venturi-type mixing nozzle 400 with a nozzle body 405 that forms a
main flow passage 410 having an inlet end 420 and a passage constriction 440 that
is illustratively provided with a plurality of lateral inlet openings 421. The Venturi-type
mixing nozzle 400 as such is shown as one example of an air-gas mixer that may be
used in an air-gas mixing unit according to the present invention. For simplicity,
the Venturi-type mixing nozzle 400 as such is embodied similar to the Venturi-type
mixing nozzle 100 of Fig. 1 to Fig. 3 so that a detailed description of the Venturi-type
mixing nozzle 400 may be omitted for brevity and conciseness.
[0045] The Venturi-type mixing nozzle 400 is illustratively provided with the plurality
of bluff bodies 150 according to Fig. 1. However, for simplicity and clarity of the
drawing only the bluff body 151 is separately labelled. Nevertheless, in contrast
to the Venturi-type mixing nozzle 100 of Fig. 1 to Fig. 3, the plurality of bluff
bodies 150 of the Venturi-type mixing nozzle 400 is neither attached to, nor integrally
formed with, the nozzle body 405. Instead, the plurality of bluff bodies 150 is now
attached to, or integrally formed with, a bluff body support 450 that is adapted to
be mounted to the nozzle body 405. By way of example, the bluff body support 450 is
ring-shaped and at least partly funnel-shaped.
[0046] Fig. 5 shows in parts (A) and (B) an air-gas mixing unit 500 comprising an air-gas
mixer 600. The air-gas mixing unit 500 may embody a combustion device which may e.g.
be used in building heating systems. The air-gas mixer 600 may be embodied similar
to the Venturi-type mixing nozzle 400 of Figure 4 and, thus, illustratively comprises
the nozzle body 405 that forms the main flow passage 410, as well as the plurality
of bluff bodies 150 having the bluff body 151, which is neither attached to, nor integrally
formed with, the nozzle body 405.
[0047] Preferably, the plurality of bluff bodies 150 is now attached to, or integrally formed
with, a bluff body plate 505. Illustratively, the bluff body plate 505 is arranged
on, and fixed to, an inlet end side 590 of the nozzle body 405.
[0048] By way of example, the plurality of bluff bodies 150 with the bluff body 151 forms
a first bluff body arrangement 510. For instance, the bluff body 151 is adapted to
enable creation of low pressure with a first degree of turbulence of a selected fluid,
such as air, in the main flow passage 410. This first bluff body arrangement 510 is
illustratively arranged in a first - in Fig. 5, part (A) upper and in Fig. 5, part
(B) lower- section 502 of the bluff body plate 505.
[0049] Furthermore, the bluff body plate 505 illustratively comprises at least one other
plurality of bluff bodies 550 that forms at least one second bluff body arrangement
520. For simplicity and clarity of the drawing, only a single bluff body of the other
plurality of bluff bodies 550 is separately labelled with the reference sign 551.
For instance, the bluff body 551 is adapted to enable creation of low pressure with
a second degree of turbulence of the selected fluid, such as air, in the main flow
passage 410. The second bluff body arrangement 520 is illustratively arranged in a
second - in Fig. 5, part (A) lower and in Fig. 5, part (B) upper- section 504 of the
bluff body plate 505.
[0050] By way of example, the first bluff body arrangement 510 is configured for use with
a first type of gas, and the second bluff body arrangement 520 is configured for use
with a second type of gas. For instance, the first type of gas may be a hydrogen gas,
and the second type of gas may be a hydrocarbon gas, such as e.g. methane.
[0051] Preferably, the bluff body plate 505 is exchangeable to enable provision of the first
bluff body arrangement 510 and/or the second bluff body arrangement 520 with the air-gas
mixer 600. Preferentially, the bluff body plate 505 is re-orientable relative to the
air-gas mixer 600 to enable positioning of the first bluff body arrangement 510 or
the second bluff body arrangement 520 on the inlet end side 590 of the air-gas mixer
600.
[0052] According to one aspect, the bluff body plate 505 may at least be flippable between
a first position and a second position relative to the air-gas mixer 600. Thus, the
first bluff body arrangement 510 may be positioned on the inlet end side 590 of the
air-gas mixer 600 in the first position, and the second bluff body arrangement 520
may be positioned on the inlet end side 590 of the air-gas mixer 600 in the second
position.
[0053] Illustratively, the first bluff body arrangement 510 is positioned on the inlet end
side 590 of the air-gas mixer 600 in a position 580 of the bluff body plate 505, as
illustrated in Fig. 5, part (A). The bluff body plate 505 may then be flipped as illustrated
with an arrow 570 such that the second bluff body arrangement 520 is positioned on
the inlet end side 590 of the air-gas mixer 600 in a position 588 of the bluff body
plate 505, as illustrated in Fig. 5, part (B).
[0054] In the example of Fig. 5, the air-gas mixing unit 500 is shown with a single air-gas
mixer, i.e. the air-gas mixer 600, as well as only two different bluff body arrangements,
i.e. the bluff body arrangements 510, 520. Thus, the bluff body plate 505 is merely
shown with a rectangular shape, by way of example. However, other shapes and overall
configurations are likewise contemplated, as described below at Fig 6.
[0055] Fig. 6 shows in parts (A) and (B) the air-gas mixing unit 500 of Fig. 5. However,
in contrast to Fig. 5 the air-gas mixing unit 500 now illustratively comprises two
air-gas mixers 600 and a circular bluff body plate 605 with two first bluff body arrangements
510 and two second bluff body arrangements 520.
[0056] According to one aspect, the circular bluff body plate 605 is rotatable between a
first position and a second position relative to the two air-gas mixers 600. Thus,
the two first bluff body arrangements 510 may be positioned on the two air-gas mixers
600 in the first position, and the two second bluff body arrangements 520 may be positioned
on the two air-gas mixers 600 in the second position.
[0057] Illustratively, the two first bluff body arrangements 510 are positioned on the two
air-gas mixers 600 in a position 680 of the circular bluff body plate 605, as illustrated
in Fig. 6, part (A). The circular bluff body plate 605 may then be rotated as illustrated
with an arrow 610 around an associated rotation axis 620 such that the two second
bluff body arrangements 520 are positioned on the two air-gas mixers 600 in a position
688 of the circular bluff body plate 505, as illustrated in Fig. 6, part (B).
[0058] Fig. 7 shows in parts (A) and (B) the air-gas mixing unit 500 of Fig. 5 with the
air-gas mixer 600 having the nozzle body 405 that forms the main flow passage 410,
as well as with the rectangular bluff body plate 505. The nozzle body 405 is illustratively
shown with a supply 710, e.g. a gas supply. The main flow passage 410 is funnel-shaped
between the inlet end 420 and the passage constriction 440, as described above at
Fig. 4, and, thus, comprises a converging inflow section.
[0059] In Fig. 7, part (A), the first bluff body arrangement 510 of the rectangular bluff
body plate 505 is arranged at the inlet end 420 of the nozzle body 405. Illustratively,
the rectangular bluff body plate 505 is adapted at the first bluff body arrangement
510 to the inlet end 420 of the nozzle body 405 and, thus, comprises a funnel-shaped
section 720 that is embodied to comply with the inlet end 420. However, the rectangular
bluff body 505 according to Fig. 7, part (A), preferably does not form a throat 810
in the converging inflow section of the main flow passage 410 between the inlet end
420 and the passage constriction 440. Instead, the throat 810 is formed by the nozzle
body 405.
[0060] In Fig. 7, part (B), the second bluff body arrangement 520 of the rectangular bluff
body plate 505 is arranged at the inlet end 420 of the nozzle body 405. However, in
contrast to part (A) the rectangular bluff body plate 505 is not adapted at the second
bluff body arrangement 520 to the inlet end 420 of the nozzle body 405 and, thus,
does not comprise a funnel-shaped section, but merely comprises a flat section 730.
Nevertheless, similar to part (A) the rectangular bluff body 505 according to Fig.
7, part (B), preferably does not form the throat 810 in the converging inflow section
of the main flow passage 410 between the inlet end 420 and the passage constriction
440, as the throat 810 is formed by the nozzle body 405.
[0061] Fig. 8 shows in parts (A) to (C) the air-gas mixing unit 500 of Fig. 7 with the air-gas
mixer 600 having the nozzle body 405 that forms the main flow passage 410, as well
as with the rectangular bluff body plate 505. The nozzle body 405 is shown with the
supply 710. The main flow passage 410 comprises the inlet end 420. However, in contrast
to Fig. 7, the main flow passage 410 does not comprise the passage constriction 440
and, thus, does not comprise a converging inflow section.
[0062] In Fig. 8, part (A), the rectangular bluff body plate 505 is provided at the first
bluff body arrangement 510 with the funnel-shaped section 720 according to Fig. 7,
part (A). Preferably, the rectangular bluff body plate 505 with the funnel-shaped
section 720 forms the throat 810 at the inlet end 420.
[0063] In Fig. 8, part (B), the rectangular bluff body plate 505 is provided at the second
bluff body arrangement 520 with the flat section 730 according to Fig. 7, part (B).
Preferably, the rectangular bluff body plate 505 with the flat section 730 forms the
throat 810 at the inlet end 420.
[0064] In Fig. 8, part (C), the rectangular bluff body plate 505 is again provided at the
second bluff body arrangement 520 with the flat section 730 according to Fig. 7, part
(B). Preferably, the rectangular bluff body plate 505 with the flat section 730 forms
a throat 820 at the inlet end 420, which is illustratively less constricting than
the throat 810 of Fig. 8, part (B).
[0065] Fig. 9 shows the air-gas mixing unit 500 of Fig. 8, part (B), with the air-gas mixer
600 having the nozzle body 405 that forms the main flow passage 410, as well as with
the rectangular bluff body plate 505. The nozzle body 405 is shown with the supply
710 and the plurality of lateral inlet openings comprising, by way of example, the
lateral inlet openings 220 of Fig. 2 and 421 of Fig. 4. The main flow passage 410
comprises the inlet end 420.
[0066] However, in contrast to Fig. 8, part (B), the rectangular bluff body plate 505 is
provided with a bluff body arrangement 910 that is preferably configured to impede
at least one of the plurality of lateral inlet openings. By way of example, the bluff
body arrangement 910 is configured to impede the lateral inlet opening 220 by enabling
a high velocity flow of the fluid, e. g. the air, that enters the main flow passage
410 via the rectangular bluff body plate 505. However, the bluff body arrangement
910 is preferably further adapted to enable creation of low pressure with a first
degree of turbulence of the fluid in the main flow passage 410 around the lateral
inlet opening 421 in a low pressure zone 920.
[0067] Fig. 10 shows the air-gas mixer 600 of Fig. 5 and Fig. 6 with the bluff body arrangement
510. However, in contrast to Fig. 5 and Fig. 6 the bluff body arrangement 510 comprises
a plurality of bluff bodies 1050 with differing shapes. For instance, four different
bluff bodies 1010, 1020, 1030, 1040 are shown, which may comprise different sizes
and inclination angles.
[0068] Preferably, the shape of the bluff bodies 1010, 1020, 1030, 1040 is optimized to
control size of a respective low pressure and low velocity zone of a respective fluid
flow, e.g. air flow, and a respective degree of turbulence induced in the fluid flow.
The optimization improves fluid mixing and reduces pressure loss across the air-gas
mixer 600 dependent on the characteristics of the gas.
1. An air-gas mixing unit (500) comprising an air-gas mixer (600) and a bluff body plate
(505), wherein the air-gas mixer (600) comprises a main flow passage (410) for mixing
a first fluid (210) with a second fluid (230) into a mixed fluid (235), the main flow
passage (410) comprising an inlet end (120) for inlet of the first fluid (210), at
least one lateral inlet opening (220, 221) for inlet of the second fluid (230), and
an outlet end (130) for outlet of the mixed fluid (235), and wherein the bluff body
plate (505) comprises at least one first bluff body arrangement (510) with at least
one first bluff body (151), and at least one second bluff body arrangement (520) with
at least one second bluff body (551), the at least one first bluff body (151) being
adapted to enable creation of low pressure with a first degree of turbulence (310)
of the first fluid (210) in the main flow passage (410) around the at least one lateral
inlet opening (220, 221), and the at least one second bluff body (551) being adapted
to enable creation of low pressure with a second degree of turbulence of the first
fluid (210) in the main flow passage (410) around the at least one lateral inlet opening
(220, 221).
2. The air-gas mixing unit of claim 1, wherein the bluff body plate (505) is exchangeable
to enable provision of different bluff body arrangements which are configured for
use with different types of gases, wherein the different bluff body arrangements comprise
different properties of optimizing mixing and pressure losses.
3. The air-gas mixing unit of claim 1 or 2, wherein the bluff body plate (505) is re-orientable
relative to the air-gas mixer (600) to enable positioning of the at least one first
bluff body arrangement (510) or the at least one second bluff body arrangement (520)
at the inlet end (120) of the air-gas mixer (600).
4. The air-gas mixing unit of claim 3, wherein the bluff body plate (505) is rotatable
or flippable between a first position (580) and a second position (588) relative to
the air-gas mixer (600), wherein the at least one first bluff body arrangement (510)
is positioned at the inlet end (120) of the air-gas mixer (600) in the first position
(580), and wherein the at least one second bluff body arrangement (520) is positioned
at the inlet end (120) of the air-gas mixer (600) in the second position (588).
5. The air-gas mixing unit of any one of the preceding claims, wherein at least one of
the at least one first bluff body arrangement (510) and the at least one second bluff
body arrangement (520) defines a throat (810) of the air-gas mixer (600) at the inlet
end (120).
6. The air-gas mixing unit of any one of the preceding claims, wherein the air-gas mixer
(600) comprises a plurality of lateral inlet openings (220, 221), and wherein at least
one of the at least one first bluff body arrangement (910) and the at least one second
bluff body arrangement (520) is configured to impede at least one of the plurality
of lateral inlet openings (220, 221).
7. The air-gas mixing unit of claim 6, wherein the at least one of the at least one first
bluff body arrangement (910) and the at least one second bluff body arrangement (520)
that is configured to impede the at least one of the plurality of lateral inlet openings
(220, 221) is embodied to enable a high velocity flow of the first fluid (210) at
the at least one of the at least one first bluff body arrangement (910) and the at
least one second bluff body arrangement (520).
8. The air-gas mixing unit of any one of the preceding claims, wherein the at least one
first bluff body (151) of the at least one first bluff body arrangement (510) and
the at least one second bluff body (551) of the at least one second bluff body arrangement
(520) are attached to, or integrally formed with, the bluff body plate (500).
9. The air-gas mixing unit of any one of the preceding claims, wherein the at least one
first bluff body arrangement (510) comprises a plurality of first bluff bodies (1050)
with differing shapes.
10. The air-gas mixing unit of any one of the preceding claims, wherein the air-gas mixer
(600) is a Venturi-type mixing nozzle with a nozzle body (405) that forms the main
flow passage (410).