FIELD OF THE INVENTION:
[0001] The present invention relates to an apparatus for burning combustible gas and a method
for using the apparatus.
BACKGROUND:
[0002] Gases containing common air pollutants, such as hydrocarbons, alcohols, ethers, soot
and other combustibles, are frequently encountered in industries wherein combustion
furnaces are utilized. In order to reduce the emission of pollutants and waste smoke
into the atmosphere, a variety of devices have been proposed for burning the combustible
gases.
[0003] A commonly utilized device is referred to as a flare stack wherein combustible gas
is burned and discharged into the open air. Several exemplary prior art techniques
are disclosed in the following patents.
[0004] U.S. Patent No. 3,828,700 to Ragot discloses an apparatus and process for the smokeless
burning of residues. The apparatus consists of a chimney designed for the introduction
of air into the burning zone, and a mechanism for introducing the residue into the
chimney in the form of a spray. Thus the disclosed apparatus and process require that
the residues to be burned off be pulverized or otherwise converted to a spray before
introduction into the chimney.
[0005] U.S. Patent No. 3,852,023 to Itoh et al. discloses an apparatus for disposing of
gas by burning. The apparatus consists of a plurality of branch pipes connected to
a main pipe carrying combustible gas. The gas is channeled into one or more of the
branch pipes according to the flow rate in the main pipe. The branch pipes are connected
to a combustion furnace having a plurality of stages arranged in vertical order, gas
introduced into the combustion furnace through the branch pipes is ignited and burned
by ignition means located in the lowermost stage of the furnace.
[0006] U.S. Patent No. 3,898,317 to Hemsath et al. discloses an incineration system for
incinerating flue gases which contain a combustible component. The system uses two
chambers that are added to a stack emitting industrial gases. The first chamber terminates
at the exit end of the stack in an annular passage so that high velocity air, which
acts as an air pump, is directed longitudinally relative to the stack. The second
chamber is disposed downstream of the first chamber and includes a plurality of burners
and a thermocouple that senses the temperature of the gases. A preset temperature
is achieved in the chambers by varying the quantities of air emitted from the first
chamber as well as the amount of fuel and air supplied to the burners in the second
chamber.
[0007] U.S. Patent No. 3,954,386 discloses a flare burner for burning combustible gases.
The flare burner consists of a venturi burner tube having specified dimensions, a
gas supply pipe having a gas outlet opening at the throat of the venturi burner tube
and pilot burner jets for burning combustion gases.
[0008] U.S. Patent No. 4,003,693 discloses a flare stack gas burner consisting of a stack
with a centrally disposed combustible gas delivery pipe having a divider with arms
for upward delivery of the combustible gas through a plurality of slots to a mixing
space. The flare stack also includes a notary diffuser for mixing the combustible
gas with air which is introduced under pressure into the stack.
[0009] It is an object of the present invention to provide a method and apparatus for burning
the combustible components of gases with the advantages which will become apparent
from the following discussion.
SUMMARY OF THE INVENTION:
[0010] The present invention relates to a method and apparatus for burning the combustible
components of gases produced in industrial processes. The method and apparatus are
particularly well suited for use in burning the combustible components of the gas
stream exiting from a carbon black furnace during the production of carbon blacks.
[0011] The apparatus of the present invention comprises:
a stack pipe having one end in communication with a gas supply pipe for receiving
a gas stream;
means for introducing air into the stack pipe to produce an air and gas mixture; a
mixing zone;
means for igniting the air and gas mixture;
means for stabilizing the ignited mixture; and
means located at the other end of the stack pipe for inhibiting downwash of the exiting
gaseous products resulting from combustion of the gas and air mixture.
[0012] The method of the present invention comprises:
introducing a gas stream containing combustible components into one end of a stack
pipe;
introducing air into the stack pipe to produce an air and gas mixture;
mixing the air and gas mixture in a mixing zone;
igniting the air and gas mixture;
stabilizing the ignited air and gas mixture; and
allowing the gaseous products resulting from combustion of the gas and air mixture
to exit the stack pipe and
inhibiting downwash of the gaseous products.
The method of the present invention is preferably performed using the apparatus of
the present invention.
[0013] The gas supply pipe refers to the pipe or conduit emitting gases produced in an industrial
process. The gas stream flows from the supply pipe into one end of the stack pipe.
In the ease of a carbon black furnace reactor, the gas supply pipe emits the gas stream
resulting from the production of carbon black. The communication between the gas supply
pipe and the end of the stack pipe in the apparatus of the present invention should
be sufficient to minimize the possibility of gas escaping into the atmosphere at,
or near, the position where the supply pipe and the stack pipe are in communication.
As explained below, in a preferred embodiment of the apparatus of the present invention,
the gas supply pipe and the stack pipe overlap.
[0014] The means for introducing air may be any means known to the art. The amount of air
introduced should be sufficient to produce an ignitible mixture of air and gas. Such
determination is within the skill of those of ordinary skill in the art. In a preferred
embodiment of the apparatus of the present invention, the means for introducing air
comprises an annular space formed between the gas supply pipe and the end of the stack
pipe, through the use of different diameter pipes.
[0015] The introduced air and the gas mix in the mixing zone. The ignitible gas and air
mixture is then ignited. The means for igniting the gas and air mixture may comprise
any means known to the art for igniting combustible gases, including, but not limited
to, pilot burners, spark generators and the like. The means for igniting may be located
at any position in the apparatus of the present invention where sufficient mixing
of the gas and air mixture has occurred to produce an ignitible mixture. Preferably,
the means for igniting is located at a position where the flame, or other igniting
means, penetrates the recirculation zone created by the means for stabilizing the
ignited gas and air mixture.
[0016] In the apparatus and method of the present invention, the ignited gas and air mixture
is stabilized to promote substantially complete burning of the combustible components
of the gas stream. The means for stabilizing the ignited gas and air mixture comprise
means for creating a recirculation zone wherein the ignited gas and air mixture recirculates.
As described below in the more detailed description of the invention, the means for
stabilizing may comprise a step between a first stack pipe that communicates with
the gas supply pipe and a second stack pipe the emits the burned gas and air mixture
into the atmosphere. The means for stabilizing may alternatively comprise an object,
preferably a cone or hemisphere, located in the interior of the stack pipe that creates
recirculation.
[0017] After combustion of the combustible components of the gas stream has been achieved,
the resultant gaseous products are emitted from the stack pipe into the atmosphere.
The emitting end of the stack pipe includes downwash inhibiting means to ensure that
the gaseous products resulting from combustion of the gas and air mixture are emitted
upwardly into the atmosphere.
[0018] The method and apparatus of the present invention advantageously burns the combustible
components of a gas stream to minimize the emission of pollutants and smoke into the
atmosphere.
[0019] Further details and advantages of the apparatus and method of the present invention
are set forth in the following more detailed description of the invention.
BRIEF DESCRIPTION OF THE DRAWINGS:
[0020]
Figure 1 depicts an embodiment of the apparatus of the present invention.
Figure 2 depicts an alternate embodiment of the apparatus of the present invention.
DETAILED DESCRIPTION OF THE INVENTION:
[0021] As set forth above, the apparatus of the present invention comprises:
a stack pipe having one end in communication with a gas supply pipe for receiving
a gas stream;
means for introducing air into the stack pipe to produce an air and gas mixture;
a mixing zone;
means for igniting the air and gas mixture;
means for stabilizing the ignited mixture; and
means located at the other end of the stack pipe for inhibiting downwash of the gaseous
products resulting from combustion of the gas and air mixture.
The apparatus of the present invention is particularly advantageous for use on the
end of smoke stacks emitting combustible gases from industrial processes.
[0022] An embodiment of the apparatus of the present invention is depicted in Figure 1.
As will be readily understood by those of ordinary skill in the art, the apparatus
shown in Figure 1 is designed to be constructed over the end of a smoke stack emitting
combustible gases.
[0023] With reference to Figure 1, the apparatus of the present invention, 1, includes a
stack pipe, 4, in communication with a gas supply pipe, 2. The inner diameter of the
gas supply pipe, 2, is shown as D1 and the inner diameter of the stack pipe, 4, is
shown as D2. The arrangement of supply pipe, 2 and stack pipe, 4 should be such that
the possibility of gas escaping into the atmosphere is minimized. In a preferred embodiment
of the apparatus of the present invention, the pipes overlap as shown in Figure 1.
In Figure 1, D1 is smaller than D2, and gas supply pipe 2, extends into stack pipe
4, thereby creating means, 5, for introducing air into the stack pipe, 4. The distance
that the pipes overlap is shown as H1.
[0024] In the embodiment of the apparatus of the present invention shown in Figure 1, the
means for introducing air into the stack pipe, 5, comprises the annular space between
the gas supply pipe, 2 and the stack pipe, 4. Air is drawn through the annular space
into the stack pipe 4. As set forth above, the amount of air drawn into stack pipe,
4 should be sufficient to produce an ignitible gas and air mixture. Such determination
is within the skill of those of of ordinary skill in the art. As also set forth above,
the means for introducing air into stack pipe, 4, may alternately comprise other means
known in the art such as an air supply pipe in communication with stack pipe, 4.
[0025] The air mixes with the gases emitted from gas supply pipe, 2, in mixing zone, 6,
to form an air and gas mixture. The length of the mixing zone should be sufficient
to allow sufficient mixing time for the introduced air and gas to produce an ignitible
air gas mixture. In Figure 1, the length of the mixing zone is shown as H2.
[0026] Stack pipe, 4, containing mixing zone, 6, communicates with one end of stack pipe,
10, having inner diameter, D3, and containing means, 14 for igniting the air and gas
mixture. Means 14, may comprise any means known to the art for igniting combustible
gases, including, but not limited to: pilot burners, spark generators and the like.
[0027] The means for igniting, 14 may be located at any position in the apparatus of the
present invention where sufficient mixing of the gas and air mixture has occurred
to produce an ignitible mixture. Preferably, the means for igniting is located at
a position wherein the flame, or other igniting means, penetrates the recirculation
zone created by the means for stabilizing the ignited gas and air mixture. In the
embodiment depicted in Figure 1, the means for igniting, 14, are located a distance
P from the end of stack pipe, 4, containing mixing zone, 6. The apparatus of the present
invention includes at least one means for igniting, and preferably includes more than
one means for igniting spaced around the periphery of stack pipe, 10.
[0028] Once the gas and air mixture has been ignited, the mixture will generally remain
burning. Thus, once ignition occurs, the means for igniting may be turned off. Preferably,
however, the means for igniting is not turned off to ensure a constant burning of
the air and gas mixture.
[0029] In the embodiment of the present invention depicted in Figure 1, D3 is greater than
D2, thereby creating step, 8, having a cross sectional width of W2. The width, W2
should be sufficient to create a stabilization zone for the ignited air and gas mixture.
Stabilization is achieved by recirculation of the ignited air and gas mixture.
[0030] The length of stack pipe, 10, is shown as H3. Preferably, the length H3 should be
sufficient to permit substantially complete combustion of the combustible components
of the ignited air and gas mixture.
[0031] The other end of stack pipe, 10, communicates with the atmosphere and includes means
for inhibiting downwash, 12, to ensure that the gaseous products resulting from combustion
of the gas and air mixture are emitted upwardly into the atmosphere. As shown in Figure
1, the means for inhibiting downwash, 12, may comprise a frustoconically flared portion
of stack pipe, 10, which increases the diameter of stack pipe, 10, to diameter D4.
The length and width of the flared portion of stack pipe, 10, which comprises the
downwash inhibiting means, are shown as H4 and W3 respectively.
[0032] The apparatus of the present invention may be constructed from materials known to
those of ordinary skill in the art. Suitable materials include, but are not limited
to: stainless steel, refractory materials and the like.
[0033] With reference to Figure 1, in the method of the present invention, gas emitted from
gas supply pipe, 2 mixes with air in mixing zone, 6. The resulting air and gas mixture
travels into stack pipe, 10 where the mixture is ignited by ignition means, 14. The
resulting ignited mixture is stabilized as a result of step, 8. The combustible components
of the air and gas mixture continue to burn in stack pipe, 10 and are discharged into
the atmosphere. Downwash inhibiting means, 12, helps to ensure that the combustion
products from the ignited gas and air mixture are emitted upwardly into the atmosphere.
[0034] Figure 2 depicts an alternate embodiment of the apparatus of the present invention.
In the apparatus depicted in Figure 2, internal flame stabilization means, 20, is
provided in stack pipe, 10. The internal flame stabilization means, 20, comprise any
object that creates recirculation, preferably a cone or hemisphere and are suspended
in the stream flowing through stack pipe 10. The remainder of the apparatus shown
in Figure 2 is similar to the apparatus shown in Figure 1 except that in the Figure
2 apparatus, the step, 8, between stack pipes, 4 and 10, has been omitted. The dimensions,
including length and internal diameter, of the stack pipes, downwash inhibiting means,
and other ports of the apparatus depicted in Figure 2, may, or may not, be the same
as those described with reference to Figure 1.
[0035] In another alternative embodiment of the apparatus of the present invention, the
apparatus is constructed with both the internal flame stabilization means, 20, and
external flame stabilization means in the form of the step, 8, between stack pipes
4 and 10.
[0036] With reference to Figure 2, in the method of the present invention, gas emitted from
gas supply pipe, 2 mixes with air in mixing zone, 6. The resulting air and gas mixture
travels into stack pipe, 10 where the mixture is ignited by ignition means, 14. The
resulting ignited mixture by stabilizing means 20. The combustible components of the
air and gas mixture continue to burn in stack pipe, 10 and are discharged into the
atmosphere. Downwash inhibiting means, 12, helps to ensure that the combustion products
from the ignited gas and air mixture are emitted upwardly into the atmosphere.
[0037] Further details of the apparatus and method of the present invention, and their advantages,
will become apparent from the following Example.
[0038] A vacuum generator Prima 600 process industrial mass spectometer, manufactured by
VG Gas Analysis System, Ltd. of the United Kingdom was utilized to determine the composition
of the gas streams referred to in the following Example. Instructions for utilizing
the spectrometer accompany the machine. The gas streams were dried to approximately
2% water, by weight, prior to analysis using Perma pure dryers, manufactured by Perma
Pure Products, Incorporated, of Toms River, New Jersey.
EXAMPLE:
[0039] This example illustrates the effectiveness of the method and apparatus of the present
invention.
[0040] An apparatus of the present invention, as depicted in Figure 1, was placed in communication
with the combustion gas stream emitted from a carbon black furnace reactor during
a carbon black production run. The apparatus of the present invention was constructed
from stainless steel and utilized a propane burner to ignite the air and gas mixture.
The geometry, and operating conditions, utilized are set forth in Table 1.
Table 1
Apparatus Geometry |
D-1 (in.) |
3.00 |
D-2 (in.) |
4.31 |
D-3 (in.) |
7.50 |
D-4 (in.) |
12.38 |
H-1 (in.) |
3.00 |
H-2 (in.) |
10.50 |
H-3 (in.) |
7.50 |
H-4 (in.) |
2.44 |
W-1 (in.) |
0.66 |
W-2 (in.) |
1.59 |
W-3 (in.) |
2.44 |
P (in.) |
1.50 |
Propane Flow to Ignitor (scfh) |
2.67 |
Ignitor Nozzle Size (in.) |
0.50 |
Feed gas Rate (kscfh) |
9.35 |
Feed gas Moisture (vol. %) |
35.3 |
Feed gas Heat Value (BTU/SCF) |
66 |
Temperature in Supply Pipe, 2 (°F) |
254 |
Stream Velocity in Supply Pipe, 2 (ft./s) |
73 |
in. = inch(es): scfh=standard cubic feet per hour; kscfh = thousand standard cubic
feet per hour vol. % = volume percentage; BTU = British thermal unit; °F = degrees
Fahrenheit; ft./s = feet per second |
[0041] The compositions of the gas streams entering and leaving the apparatus of the present
invention were determined, after drying, according to the procedures described herein.
The results are set forth in Table 2 below:
Table 2
Dried Gas Stream Composition |
Compound |
Entering Stream |
Exiting Stream |
N2 (vol. %) |
62.50 |
84.18 |
O2 (vol. %) |
3.56 |
0.00 |
CO2 (vol. %) |
2.44 |
13.61 |
Ar (vol. %) |
0.67 |
0.99 |
C2H2 (vol. %) |
0.223 |
<0.003 |
H2 (vol. %) |
14.99 |
0.18 |
CO (vol. %) |
14.55 |
0.82 |
CH4 (vol. %) |
0.772 |
<0.003 |
H2S (ppmv) |
626 |
<31 |
SO2 (ppmv) |
631 |
2249 |
CS2 (ppmv) |
959 |
<15 |
COS (ppmv) |
233 |
<15 |
vol. % = volume percentage; ppmv = volume parts per million |
The results provided in Table 2 indicate that the method and apparatus of the present
invention reduce the emission levels of all of the combustible components, including
CS
2, COS, and H
2S in the gas stream. These results also make it apparent that the combustion efficiency
of the apparatus of the present invention is high.
[0042] These results indicate that the method and apparatus of the present invention are
advantageous for use in burning the combustible components of gases.
[0043] It should be clearly understood that the forms of the present invention herein described
are illustrative only and are not intended to limit the scope of the invention.