U.S. patent number 3,857,669 [Application Number 05/177,399] was granted by the patent office on 1974-12-31 for catalytic heater head.
This patent grant is currently assigned to Impala Industries, Inc.. Invention is credited to Robert I. Schantz, Jay N. Smith.
United States Patent |
3,857,669 |
Smith , et al. |
December 31, 1974 |
CATALYTIC HEATER HEAD
Abstract
A catalytic heater head having a back pan forming a gas
diffusion chamber behind a layer of catalytic mass; the back pan
being rectangular shape with a central gas receiving port and a
plurality of channels radiating outwardly therefrom to reservoirs
located in the four corners of the pan.
Inventors: |
Smith; Jay N. (Wichita, KS),
Schantz; Robert I. (Burien, WA) |
Assignee: |
Impala Industries, Inc.
(Wichita, KS)
|
Family
ID: |
22648448 |
Appl.
No.: |
05/177,399 |
Filed: |
September 2, 1971 |
Current U.S.
Class: |
431/328 |
Current CPC
Class: |
F23D
14/18 (20130101) |
Current International
Class: |
F23D
14/18 (20060101); F23d 013/14 () |
Field of
Search: |
;431/328,329
;239/522,523,524,568 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Perlin; Meyer
Assistant Examiner: Capossela; Ronald C.
Claims
Having described the invention will sufficient clarity to enable
those familiar with the art to construct and use it, we claim:
1. A catalytic heater head for use with gaseous fuels,
comprising:
a gas impervious rectangular back pan shaped to define a shallow
gas diffusion chamber with an open front side;
a fibrous layer of catalytic-coated mass mounted on the front side
of said back pan;
a gas emitter head centrally located in said back pan and including
at least one orifice located to emit gas in a directed stream;
means to supply gas to said emitter head; and
said back pan being formed with separate reservoirs in each of the
four corners thereof and channel means radiating outward from the
gas emitter head terminating in at least one of the reservoirs, the
volume of the channel means being substantially smaller than the
volume of the reservoirs, the channel means being substantially
aligned with the gas stream from the emitter head whereby the
flowing gas is partially confined as it travels upward through the
channel means into the respective reservoir and ridge means
separating each of the reservoirs partially restricting the flow of
gas between the reservoirs.
2. Apparatus according to claim 1, wherein the channel means
includes a pair of channels each extending into a separate
reservoir at an upper corner of the back pan, and the emitter head
includes two orifices each directing a gas stream into one of the
said channels.
3. Apparatus according to claim 1, wherein the back pan is formed
to include a recessed center area surrounding the gas emitter head
into which the channel means terminate.
4. Apparatus according to claim 1, wherein the reservoirs decrease
in depth as they extend away from the corners of the back pan.
5. Apparatus according to claim 1, wherein the reservoirs decrease
in depth as they extend away from the corners of the back pan
terminating in said ridges which separate each reservoir.
6. Apparatus according to claim 1, wherein the channel means
includes a pair of channels each extending into a separate
reservoir at an upper corner of the back pan, and the emitter head
includes two orifices each directing a gas stream into one of the
said channels, and a ridged layer of pervious material sandwiched
between the layers of catalytic mass and the back pan to prevent
the catalytic mass from deforming into the reservoirs and channels
of the back pan.
7. Apparatus according to claim 1, wherein the channel means
includes a pair of channels each extending into a separate
reservoir at an upper corner of the back pan, and the emitter head
includes two orifices each directing a gas stream into one of the
said channels, and a filter pad of ceramic fibrous material
positioned under the layer of catalytic mass and a rigid layer of
pervious material sandwiched between the filter pad and the back
pan to prevent the fibrous layers from deforming in the reservoirs
and channels of the back pan.
8. Apparatus according to claim 1, wherein the channel means
includes separate channels to each of the four reservoirs, the
emitter heads including two primary orifices and two secondary
orifices, the primary orifices each directing a gas stream downward
into the two lower reservoirs while the secondary orifices are
directed to the upper two reservoirs.
Description
BACKGROUND OF THE INVENTION
It is well known that thermonic elements which function by
catalytic oxidation of gas can afford satisfactory results only
when a very uniform feeding of the gas is effected over the whole
internal area of the catalytic mass. Whenever a catalytic head of
the type shown in the present invention is vertically positioned,
the heavier than air gas entering the back pan has a tendency to
settle at the bottom of the pan before coming through the catalytic
mass. This causes the unit when operating, to generate heat only in
the lower portions of the catalytic element, which severely limits
its overall heating capacity. If the gas used is lighter than air,
such as natural gas, the problem is reversed with the gas gathering
at the top portions of the catalytic element. Another type back pan
design, shown in U.S. Pat. No. 3,073,379, has attempted to effect
uniform flow of gas to the catalytic mass by the usage of an
arcuate shaped manifold pipe having a series of small holes therein
which emit the gas onto the catalytic element. This type of unit
has been found to be very complex in structure and expensive to
produce, and also, it does not achieve uniform distribution.
SUMMARY OF THE INVENTION
The catalytic heater head of the present invention employs a single
gas emitter head with a back pan shaped with upwardly and
downwardly directed channels and reservoirs at the corners thereof
to better effect a more even gas distribution over the entire area
of the catalytic element.
The primary object of the present invention is to provide a planar
shaped catalytic heater head which effects even distribution of the
gas through the catalytic mass.
A further object of the present invention is to provide a catalytic
heater head with a maximum heat output for a minimum size catalytic
mass.
Another object of the present invention is to provide a back pan
design which replaces complex manifold structures for providing
even gas distribution through the catalytic mass.
Another object of the present invention is to provide a head which
utilizes heavier and lighter than air gases.
The invention, and its various objects and advantages, will be more
clearly understood when the following description is read in
connection with the accompanying drawings in which:
FIG. 1 is a plan view of the heater head with portions of the
fibrous ceramic elements broken away to view the back pan
structure;
FIG. 2 is a sectional view taken along lines 2 -- 2 of FIG. 1;
FIG. 3 is a section taken along lines 3 -- 3 of FIG. 1 with
portions of the outer frame and protective grate broken away;
FIG. 4 is a fragmentary section to an enlarged scale, taken along
lines 4 -- 4 of FIG. 1 with a gas supply symbolically shown;
and
FIG. 5 is a gas emitter head of a different embodiment.
In referring to FIG. 1, the catalytic heater head of the present
invention is generally described by reference numeral 10. The head
10 includes a metal back pan 12 shaped to form a gas diffusion
chamber behind the catalytic elements. Formed at each of the four
corners of the back pan 12 are reservoirs or pockets 14, 15, 16 and
17, the latter two not being visible in FIG. 1. While the outer
sides of reservoir 14 are clearly delineated by walls 18 and 19,
the inner limits of reservoir 14 are defined by a gradually sloping
bottom surface which terminates in a ridge 20 between reservoirs 14
and 15. A similar ridge 21 separates reservoirs 14 and 17. The
reservoirs 16 and 17 on the right side of pan 12 are identical to
reservoirs 14 and 15. Formed in the center of back pan 12 is a
circular recessed area 32 which contains a gas emitter head 22.
Radiating outward from the recessed area 32 are four channels 24
which connect the center area with each of the separate reservoirs
previously mentioned. The gas emitter head 22 has a pair of
orifices 25, each one being aligned with a channel 24 so that the
gas stream emitted from the orifices will be enclosed by the
channels 24 until the gas reaches the outer reservoirs 14 and 17.
In viewing FIG. 4, the gas emitter head 22 passes through an
opening in the back pan 12 and is held in place by a sealing nut
and washer 27. The threaded fitting 28 on the emitter head is a
standard fitting which can be attached to any conventional gas
line. A tank 29 is symbolically shown supplying gas to the head
through a regulator valve 30.
Positioned inside the back pan 12 is a rectangular piece of
expanded metal 34 which prevents the pliable fibrous elements 40
and 42 from deflecting into the cavaties of the back pan. The
expanded metal 34 is held in place by a weld 36. Surrounding the
periphery of back pan 12 is an extended lip 37 which terminates in
an upstanding flange 38. Positioned on top of the expanded metal 34
is a fibrous filter pad 40 made up of alumina-silica fibers. Pad 40
is manufactured under the trademark of "Kaowool," manufactured by
the Babcox Wilcox Co., or "Fiberfrax" manufactured by the
Carborundum Company. Positioned on top of the pad 40 is a thinner
vacuum cast pad 42 formed of an alumina-silica fiber coated with a
catalyst such as platinum. Both pads 40 and 42 have sufficient
porosity for the gas to flow therethrough with a very low pressure
in the back pan. The filter pad 40 can be eliminated with the usage
of a single pad 42. Holding the two ceramic pads 40 and 42 in
sealing engagement with lip 37 of the back pan is an outer frame
45. Covering the outer frame 45 and extending outwardly therefrom
is a wire protective grate 46 which protects persons from touching
the hot catalytic element 42.
OPERATION
The heating head 10 is generally used in a near vertical position.
If it is tilted downward it has a minimum angle requirement of 15
percent from the horizontal to allow the by-products of combustion
to escape. When using propane as a fuel, the head is positioned as
seen in FIG. 1 with the reservoirs 14 and 17 at the top of the head
so the gas streams from orifices 25 will be directed to the upper
two reservoirs. As the gas flows out from orifices 25, the channels
24 tend to confine it into its respective reservoir 14 or 17. While
a portion of the gas may find its way between the openings in the
expanded metal 34, down to the lower reservoirs 15 and 16, most of
the gas will be retained in its upper reservoirs 14 and 17 until it
flows out through the catalytic element. The deep corners of the
reservoir tend to improve the gas flow through the catalyst element
at the corners. When using natural gas as a fuel, the gas emitter
head 22a, shown in FIG. 5, is utilized. Since natural gas is
lighter than air, the primary gas orifices 52 are directed downward
to the lower two reservoirs 15 and 16. While some of the gas from
orifices 52 will rise above the lower reservoirs, the additional
smaller secondary orifices 54 are necessary to accumulate a
sufficient amount of gas in the upper reservoirs.
* * * * *