U.S. patent number 3,672,648 [Application Number 05/093,274] was granted by the patent office on 1972-06-27 for tuyere assembly.
Invention is credited to Franklin Carr Price.
United States Patent |
3,672,648 |
Price |
June 27, 1972 |
TUYERE ASSEMBLY
Abstract
A tuyere for controlling flow through a hole in a flat reactor
hearth which utilizes the Bernoulli effect to retain its position.
The tuyere is essentially a flat disc with a centering shaft
fitting loosely in the hearth hole to prevent sideways movement.
Either metal, including sheet metal, or refractory material can be
used to form the tuyere, and it can be shaped to completely block
backflow or with port grooves to increase gas volume flow.
Inventors: |
Price; Franklin Carr (Chicago
Heights, IL) |
Family
ID: |
22238058 |
Appl.
No.: |
05/093,274 |
Filed: |
November 27, 1970 |
Current U.S.
Class: |
422/143; 34/237;
266/172; 110/264; 432/192; 34/576 |
Current CPC
Class: |
B01J
8/44 (20130101) |
Current International
Class: |
B01J
8/24 (20060101); B01J 8/44 (20060101); F27b
015/00 () |
Field of
Search: |
;263/21A
;34/57R,57A |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Camby; John J.
Claims
I claim as my invention:
1. In a fluidized bed reactor having a wind box and a reaction
chamber, the combination comprising, a substantially horizontal
hearth separating the wind box from the reaction chamber, said
hearth having a flat top surface and an opening extending from the
wind box through said flat surface with no peripheral lip, and a
tuyere for controlling flow through the opening, said tuyere having
a substantially flat body on said surface overlying the opening and
being at least approximately twice the size of said opening, said
body having a stop surface cooperating with a portion of the hearth
to prevent lateral movement of the body from said opening, the flow
through said opening and against said body being substantially
unimpeded so that said flow after striking said body expands
radially and increases in velocity between the body and said flat
surface to develop a force holding the tuyere in place.
2. The combination of claim 1 in which said opening and said tuyere
body are substantially circular and the face of the body contacting
said surface is recessed in its center portion, said stop surface
being defined by a shaft on said body extending from the
approximate center of said recess down into said opening.
3. The combination of claim 2 in which said contact face includes
an unbroken periphery resting on said hearth surface without
creating a gap between the tuyere and the hearth.
4. The combination of claim 2 in which said contact face is formed
with a port groove extending radially from said recessed center
portion.
5. The combination of claim 4 in which said groove extends through
the periphery of said body.
Description
DESCRIPTION OF THE INVENTION
This invention relates generally to fluidized bed reactors and more
particularly concerns an improved tuyere and hearth for such
reactors.
A fluidized bed reactor includes a flat, horizontal hearth for
supporting a mass of material forming the bed. A combustion chamber
beneath the hearth supplies gas which flows through holes in the
hearth to reach the bed. Conventionally, tuyeres are placed at the
upper ends of the hearth holes to control the gas flow and prevent
undesirable downward movement of the bed material. Hearth and
tuyeres are formed both of metal, which is more economical, and
refractory material, which is suitable for higher reactor
temperatures.
A primary aim of the invention is to provide a tuyere and hearth
which operate on a principal permitting great performance
versatility to result from making minor changes in tuyere
configuration. A related object of the invention is to provide a
tuyere and hearth as characterized above which allows easy,
economical tuyere installation and removal, since no cement or
fasteners are required, so that tuyeres of varying characteristics
can be readily substituted for one another.
A further object is to provide a tuyere and hearth of the above
character which can be readily formed to deliver widely varying gas
volumes without altering driving pressures, and to completely
eliminate backflow of the bed material upon shutdown when that
feature is desired.
It is also an object of the invention to provide a tuyere and
hearth of the above kind which is virtually clog-proof in
operation, and which facilitates cleaning out the bed material
after an operating campaign.
Another object is to provide a tuyere as referred to above which is
economical to manufacture, having a basically simple shape, and
which, depending upon temperature requirements, can be formed of
either refractory material or metal, including economical metal
sheet material.
Other objects and advantages of the invention will become apparent
upon reading the following detailed description and upon reference
to the drawings, in which:
FIG. 1 is a fragmentary vertical section taken through a refractory
hearth constructed in accordance with the invention;
FIG. 2 is an enlarged fragmentary plan taken approximately along
the line 2--2 in FIG. 1;
FIG. 3 is a further enlarged fragmentary vertical section showing a
portion of the structure illustrated by FIG. 1;
FIG. 4 is a still further enlarged section similar to FIG. 3 but
showing a modified form of the invention;
FIG. 5 shows a plan taken approximately along the line 5--5 of FIG.
4;
FIG. 6 is similar to FIG. 3 but shows a further modification of the
invention;
FIG. 7 is similar to FIG. 1 and shows a modification embodying the
invention;
FIGS. 8 and 9 are similar to FIG. 3 but show, respectively, further
modifications embodying the invention; and
FIG. 10 is similar to FIG. 2 and is taken approximately along the
line 10--10 of FIG. 7.
While the invention will be described in connection with a number
of preferred embodiments, it will be understood that I do not
intend to limit the invention to those embodiments. On the
contrary, I intend to cover all alternatives, modifications and
equivalents as may be included within the spirit and scope of the
invention.
Turning first to FIGS. 1 and 2, there is shown a fluidized bed
reactor 10 having a cylindrical metal shell 11 lined with
refractory material 12 and being divided by a substantially
horizontal hearth 13 which defines and separates a lower windbox 14
and an upper reaction chamber 15. In the illustrated construction,
the hearth 13 consists of refractory blocks 16 cut and assembled to
create a circular masonry arch having a flat upper surface 17
supported at its periphery by a collar structure 18. The blocks 16
are formed with complementary grooves so that adjacent blocks
establish substantially circular openings 19 extending from the
windbox 14 through the surface 17 to the reaction chamber 15.
As will be familiar to those skilled in this art, the fluidized bed
in the reaction chamber 15 is created by transmitting gas, usually
at high temperatures, through the hearth 13 from the windbox 14. By
maintaining a vertical gas flow across the entire bottom of the
reaction chamber 15 the material in the chamber is fluidized for
purposes of the desired reaction.
In accordance with the invention, flow through the openings 19 is
controlled by individual tuyeres 20 overlying each opening, each
tuyere comprising a substantially flat body 21 resting on the
surface 17 which is approximately twice the size of the opening and
which has a stop surface cooperating with a portion of the hearth
to prevent lateral movement of the body from the opening (see FIG.
3). Preferably, the tuyeres 20 are circular, as are the openings
19, with a lower face 22 contacting the hearth surface 17 and being
formed with a recess 23 in the center portion of the surface 22
from which a shaft 24 extends downwardly into the underlying
opening 19 so as to define the tuyere stop surface. The pressure of
the gas flow from the windbox 14 through the openings 19 will cause
the tuyere body 21 to rise slightly above the hearth surface 17 so
that gas can escape into the reaction chamber 15 between the hearth
surface 17 and the contact face 22 of the tuyere. In the typical
operating campaign, measurements indicate that a clearance of about
0.020 to 0.030 inch is created between the surface 17 and the face
22 with there being a small amount of constant fluttering of the
tuyere. This latter phenomena has been found effective to keep the
gas flow uniform since it avoids accumulated material from the
reaction bed plugging up the hearth openings.
The effectiveness of the tuyeres 20 depends upon the Bernoulli
effect, that is, the fact that pressure in a stream of fluid is
reduced as its velocity is increased. In this instance, the gas
flow through the openings 19 from the windbox 14 not only increases
in velocity as it escapes between the surface 17 and the face 22
but also expands radially beneath the tuyeres, both factors
creating lesser pressures beneath the tuyeres tending to hold the
tuyeres onto the hearth surface 17. It has been found that this
effect obtains when the tuyere diameter is approximately at least
twice the size of the opening which it is controlling. The holding
force created by the Bernoulli effect is actually increased upon
increasing the gas flow rates through the openings 19. Lateral
movement of the tuyeres is prevented by engagement of the stop
surface shafts 24 with the sides of the respective openings 19.
Slight modifications to the shape of the tuyeres can be made for
achieving certain desired results. For example, gas flow can be
greatly increased by forming port grooves in the tuyere hearth
contact face. In FIG. 4 there is shown a modified tuyere 20a
embodying the invention and having a body 21a, center recess 23a
and stop surface shaft 24a together with a plurality of radial port
grooves 30. As in the tuyere 20, the tuyere 20a has an unbroken
periphery around the recess 23a adapted to contact the hearth
surface 17. This eliminates the possibility of backflow from the
fluid bed through the opening 19 when the reactor is first shut
down.
If even greater gas flow into the bed is desired, the radial ports
in the tuyeres can extend through the tuyere periphery, as do the
ports 30b in the tuyere 20b shown in FIG. 6. Otherwise, the tuyere
20b includes a body 21b, a center recess 23b and a stop surface
shaft 24b corresponding to the similar parts previously
described.
An important aspect of the invention lies in the ability to replace
the tuyeres readily for an alternate design having slightly
differing operating characteristics. For example, it is merely
necessary to lift the tuyeres 20 from the reactor 10 and replace
them with a set of tuyeres 20a or 20b, with the latter being merely
dropped into position. No fasteners, adhesives or cements are
required and the hearth is not disturbed. Because of the basically
flat shape of the tuyeres, they extend only a short distance into
the reaction chamber and an essentially flat surface is presented
when it is necessary or desirable to clean out the fluidized
bed.
The tuyeres already described are preferably formed in one piece of
refractory material for use in a high temperature, refractory lined
reactor of the type represented by the reactor 10. The invention is
also susceptible of use in lower temperature, and also lower cost,
metal reactors of the type represented by the reactor 10b shown in
FIGS. 7 and 10. Here, a metal reactor shell 11b surrounded by
insulating material 35 supports a flat metal plate hearth 13b on a
collar structure 18b, with the hearth 13b being pierced by a
plurality of holes or openings 19b for admitting gas from a windbox
14b to a reaction chamber 15b. The tuyeres 20c, made of sheet
metal, control gas flow through the openings 19b and include a body
21c formed to define a center recess 23c through which extends a
shaft 24c constituting the tuyere stop surface (see also FIG. 8).
The tuyere 20c functions as do the tuyeres previously described but
it can be appreciated that the sheet metal configuration provides a
particularly economical construction.
An alternate tuyere form, (FIG. 9), provides a tuyere 20d of formed
sheet material having radial ports 30d for increasing the gas flow.
The ports 30d function as do the previously described radial
ports.
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