Information
-
Patent Grant
-
6537064
-
Patent Number
6,537,064
-
Date Filed
Thursday, May 4, 200024 years ago
-
Date Issued
Tuesday, March 25, 200321 years ago
-
Inventors
-
Original Assignees
-
Examiners
- Bennett; Henry
- Cocks; Josiah
Agents
- Bittman; Mitchell D.
- Lemack; Kevin S.
-
CPC
-
US Classifications
Field of Search
US
- 431 354
- 431 351
- 431 350
- 431 185
- 431 159
- 431 181
- 431 182
- 431 175
- 431 8
- 431 9
- 239 399
- 239 403
- 239 419
- 239 566
- 239 557
- 239 432
- 060 749
-
International Classifications
-
Abstract
A burner having improved flame quality even at high turn-down ratios. The burner includes a flow director which is preferably a bent sheet or plate positioned in the burner to alter the flow geometry of the air component into a series of channels where the air mixes with the fuel. Preferably the flow director is perforated, the perforations providing a second avenue for the flow of air into the mixing channel.
Description
BACKGROUND OF THE INVENTION
The present invention relates to burners, in particular, line burners for use in web supporting and drying apparatus, although other applications are within the scope of the invention.
According to conventional combustion science, each type of burner flame (e.g., premix flame, diffusion flame, swirl flame, etc.) burns with a different optimal stoichiometric mix of fuel to combustion air, by which low emission concentrations in the burner flue gas appear. It is therefore important to control or maintain the desired optimal stoichiometry of the burner. Failure to closely regulate the burner air/fuel ratio over the range of burner output can lead to poor flame quality and stability (flameout, yellow flames, etc.) or excessive pollution (high NO
X
, CO).
The turn-down ratio of a burner is the ratio of a maximum firing rate to a minimum firing rate for a particular burner, where firing rate is the measure of the amount of fuel gas consumed per hour, such as BTU/hour. A high turn-down ratio is preferred, since this indicates that the burner is consuming less fuel at the minimum firing rate.
U.S. Pat. No. 5,662,467, the disclosure of which is hereby incorporated by reference, discloses a nozzle mixing line burner having a combustion chamber and a nozzle body having two channels, each of which receives air and fuel. The mixture of air and fuel from each channel is discharged into the combustion chamber where they are mixed. However, at most turned-down firing conditions (i.e., low firing rates), mixture is inadequate and flame quality is diminished.
It would therefore be desirable to improve the flame quality of line burners especially at low firing rates.
SUMMARY OF THE INVENTION
The problems of the prior art have been overcome by the present invention, which provides a burner having improved flame quality even at high turn-down ratios or low firing rates. The burner includes a flow director which is preferably a bent sheet or plate positioned in the burner to alter the flow geometry of the air component into a series of channels where the air mixes with the fuel. Preferably the flow director is perforated, the perforations providing a second avenue for the flow of air into the mixing channel.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1
is a perspective view of a line burner in accordance with the present invention;
FIG. 2
is cross-sectional view of a line burner in accordance with the present invention;
FIG. 3
is a section view of the flow director for the burner in accordance with the present invention;
FIG. 4
is a schematic view showing air flow in a burner in accordance with the present invention;
FIG. 5
is a schematic view showing air flow in a burner in accordance with the prior art;
FIG. 6
is a schematic view showing air flow in a burner in accordance with an alternative embodiment of the present invention; and
FIG. 7
is a cross-sectional view of a flow director in accordance with a preferred embodiment of the present invention.
DETAILED DESCRIPTION OF THE INVENTION
Turning first to
FIG. 2
, a nozzle body
18
is shown having a fuel distribution chamber
20
, two rows of opposing fuel/air mixing channels
22
,
24
, and one or more fuel passages
26
,
28
providing communication between fuel-distribution chamber
20
and each mixing channel
22
,
24
. The nozzle body is preferably constructed of iron and is unitary, although other materials such as aluminum or sheet metal can be used. Fuel is dispersed from the fuel distribution chamber
20
, which has a triangular cross-section, into each mixing channel
22
,
24
by the respective fuel passages
26
,
28
, as shown by the arrows
69
in FIG.
2
. The channels
22
,
24
are angled and converge towards a combustion chamber defined by opposite side walls
63
(
FIG. 5
, only one side wall shown) attached to the nozzle body
18
so that the flame
17
fires into the combustion chamber. This burner design is that disclosed in U.S. Pat. No. 5,662,467 and familiarity therewith is assumed.
As illustrated in
FIG. 5
, nozzle body
18
of burner
10
includes two rows of opposing angled fuel/air mixing channels
22
(only one shown) which extend between spaced front and back faces
30
,
32
of the nozzle body
18
. Air enters channels
22
,
24
in a predominantly parallel direction relative to the outer walls of each channel
22
,
24
as shown by arrows
97
. In contrast, fuel passage
26
communicating with each channel
22
,
24
is located along the innermost side of each angled channel
22
,
24
. As a result, there is an impingement zone
17
where the air and fuel mix to provide flame stability. However, evaluation of the burner in operation indicates that the flame
41
has regions where the flame is not well established. The voids within the flame
41
are most obvious at locations where the fan could most easily force the air through the nozzle body
18
, suggesting a location where the mix of air and fuel is not optimal, or the air flow through body
18
is not uniform.
In order to ensure adequate mixing of the air and fuel components and uniform air flow,
FIGS. 1 and 2
show the placement of a flow director
118
in the nozzle body
18
upstream of the inlets to the channels
22
,
24
in order to direct the flow of air into one or preferably both of the rows of mixing channels
22
,
24
in accordance with the present invention. The flow director
118
forces the air
121
to distribute along an air gap
122
(
FIG. 1
) created between each leg
38
of the nozzle body
18
(which leg
38
can be unitary with the nozzle body or coupled thereto by any suitable means known to those skilled in the art, such as welding or riveting, and which also can serve as a mounting wall for an air housing) and the free flange end
45
of each flow director
118
. This gap
122
extends in the longitudinally direction along the entire length of the flow director
118
. In addition, a plurality of apertures
119
are formed in the flow director
118
, which apertures
119
also allow source air
120
to enter each channel
22
,
24
. Preferably the apertures are circular and evenly spaced as shown, although other shapes can be used. The apertures
119
should align with corresponding apertures in the nozzle body
18
providing entry into the channels
22
,
24
. The air gap
122
is preferably at least as wide as the diameter of the apertures
119
. It is most preferably ⅜ of an inch wide.
As illustrated in
FIG. 4
, primary air
121
is sheltered by the redistribution zone
123
defined by the flow director
118
and the nozzle body
18
. Secondary air
120
is a smaller air component relative to primary air
121
, and is traveling in a well-defined direction when discharged through apertures
119
. The primary air
121
is quieted by redistribution zone
123
, and flows to fill in around the discharge of secondary air
120
as shown in FIG.
3
. The secondary air
120
, which has a velocity, assists the primary air
121
in flowing into the channels
22
,
24
and combines with the primary air
121
.
Comparing the area of the secondary holes
119
to the combined slot and hole area, it is found that this ratio is 0.23. Thus, it is expected that about ¼ of the flow into the channel
22
is from the secondary holes
119
. If a separate, high pressure air source were used to supply the secondary air to holes
119
, then a much smaller amount of area, about 5%, could be used since the higher pressure would give the secondary air a much higher velocity. The amount should be less than 50%, however. If the holes provide too much flow, the flow may stratify on the opposite wall.
The flow director
118
causes the air
97
to assume a general directionality more like the path of the fuel/air mixing channels
22
,
24
. Flow director
118
promotes the resulting focused air
124
to mix with the fuel
69
at the end of fuel passages
26
,
28
before the mixture leaves the air/gas mixture zone
125
in each of the channels
22
,
24
. Although the present invention should not be so limited, it is believed that the improved mixing is due to the following phenomenon. Since the fuel
69
voids from fuel passages
26
,
28
with some velocity, the best mixing potential is found where the fuel is just leaving passages
26
,
28
due to cross-velocity with the impinging air. By focusing the air
124
to generally flow along the innermost side of the channels
22
,
24
, the air is available to mix with the fuel in the most ideal location for intimate and complete mixing. The arrows in
FIG. 4
illustrate the respective flows of the air
125
and fuel
69
, in contrast to the prior art flow of
FIG. 5
where the air
97
is predominantly aligned toward the outermost side of the channels
22
,
24
. Since the volume of air
97
is larger than the volume of fuel
69
, the air tends to force the fuel volume toward the innermost side, leaving a two component, mostly stratified and laminar flow where the fuel has little opportunity to mix early on with the air in the prior art device.
Flow director
118
is preferably constructed of 20 ga steel, formed into a generally inclined cross-section with a multiple of bends or steps. The preferred configuration is illustrated in the drawings, particularly
FIG. 7
, and includes a first free flange end
45
which is substantially parallel to nozzle leg
38
; a first bent section
46
extending substantially orthogonally from the flange end
45
; a second bent section
47
extending substantially orthogonally from first bent section
46
and being substantially parallel to nozzle leg
38
, the second bent section being longer than the first free flange end
45
; a third bent section
48
extending substantially orthogonally from the second bent section
47
, the third bent section
48
having formed therein a plurality of spaced apertures
119
in the direction along the longitudinal direction of the nozzle
18
, the third bent section
48
being shorter than the first bent section
46
; a fourth bent section
49
extending from the third bent section in a direction substantially parallel to the channel
22
; and a fifth bent section
50
extending from the fourth bent section
49
in a direction substantially orthogonal to the nozzle leg
38
. The fifth bent section
50
is attached to nozzle body
18
between the fuel distribution chamber
20
and channel
22
by any suitable means, such as welding, screwing, riveting or trapping with an end cap. Preferably the flow director
118
extends longitudinally along each side of nozzle body
18
to serve a majority of the channels
22
,
24
with a distributed air flow
124
. Most preferably, the flow director
118
extends longitudinally along each side of nozzle body
18
to serve all of the channels
22
,
24
, with the provision for a gap in flow director
118
to provide access for the burner ignition and flame supervision devices to pass through. In the preferred embodiment, the flow director
118
is 2.125 inches long and {fraction (13/32)} inches high, and the apertures
119
are ⅜ inch diameter holes spaced on 1 inch centers.
The flow director
118
can be formed as an integral part of the nozzle body
18
, or can be a separate sheet attached during or after construction of the nozzle body
18
.
FIG. 6
illustrates an alternative embodiment of the flow distributor of the present invention. In this embodiment, redistribution of air and proper mixing is accomplished by one or more perforated plates
90
, and the optional use of a deflector or swirl producing device
92
. The perforated plate(s)
90
have a series of spaced apertures
91
positioned along their length. In the preferred design, the open area (per foot of burner length) of the plate
90
is between about 5-40%, more preferably 10-20%, most preferably about 15.2% for a single plate. If multiple plates are used, then an open area of about 40 to about 75% would be effective, preferably about 60% to about 65%.
The deflector
92
is a bent sheet positioned at the elbow
95
of the nozzle body
18
as shown. It functions to deflect the incoming air in the direction of the arrows and promotes uniform mixing in the passageway
22
. The length of the free end
93
of the deflector
92
can be readily determined by those skilled in the art for optimal mixing.
Desirable turn-down ratios are 10-20, which allow stable minimum firing rates.
Claims
- 1. A burner comprising a nozzle body having a front face and a back face spaced from said front face, said back face being in communication with an air supply and with a fuel supply, said nozzle body comprising:a channel between said front face and said back face, said channel having an air inlet for receiving air from said air supply and having a fuel inlet receiving fuel from said fuel supply, and at least one flow director positioned upstream of said air inlet, said flow director directing the flow of air into said air inlet to mix said air supply with said fuel in said channel; said flow director having a free end, a first bent portion extending from said free end, a second bent portion extending from said first bent portion, a third bent portion extending from said second bent portion, a fourth bent portion extending from said third bent portion, and a fifth bent portion extending from said fourth bent portion and being coupled to said nozzle body.
- 2. The burner of claim 1, wherein said nozzle body further comprises opposite sides extending from said back face, and wherein said at least one flow director defines with one of said opposite sides a redistribution zone for flow of said air supply prior to said air supply entering said inlet.
- 3. The burner of claim 1, wherein said flow director comprises a plurality of apertures.
- 4. The burner of claim 1, wherein said third bent portion comprises a plurality of apertures.
- 5. The burner of claim 1, wherein each of said bent portions is bent at an angle of about 90°.
- 6. A burner comprising a nozzle body having a front face and a back face spaced from said front face, said back face being in communication with an air supply-and a fuel supply, said nozzle body comprising:two rows of a plurality of channels between said front face and said back face, each said channel having an air inlet for receiving air from said air supply and having a fuel inlet for receiving fuel from said fuel supply, and a flow director positioned upstream of each said air inlet, each flow director directing the flow of air into each said air inlet to cause said air to mix with said fuel in each of said channels; said flow director having a free end, a first bent portion extending from said free end, a second bent portion extending from said first bent portion, a third bent portion extending from said second bent portion, a fourth bent portion extending from said third bent portion, and a fifth bent portion extending from said fourth bent portion and being coupled to said nozzle body.
- 7. The burner of claim 6, wherein said third bent portion comprises a plurality of apertures.
- 8. The burner of claim 6, wherein each of said bent portions is bent at an angle of about 90°.
US Referenced Citations (24)
Foreign Referenced Citations (1)
Number |
Date |
Country |
1 591 994 |
Jun 1970 |
FR |