U.S. patent number 3,590,909 [Application Number 04/872,228] was granted by the patent office on 1971-07-06 for oxygen boiler.
This patent grant is currently assigned to The Trane Company. Invention is credited to Alan G. Butt.
United States Patent |
3,590,909 |
Butt |
July 6, 1971 |
OXYGEN BOILER
Abstract
An oxygen reboiler is provided with a brazed plate fin-type heat
exchanger at least partially submersed in a body of liquid oxygen.
The flat vertical oxygen passages thereof are open at the top and
bottom and have no fins or other separate extended heat transfer
surface therein which may tend to cause accumulations of hazardous
acetylene. These passages are closed at their vertical edges to
promote percolator action of the liquid oxygen therein when heated
by nitrogen passing through adjacent passages. The conventional
closing bar or other elongated member normally brazed between plate
surfaces to close these vertical edges has been substantially
eliminated from the oxygen passages to thereby reduce the diffusion
of molten braze metal onto the plate surfaces thereof. The vertical
edges of these passages have been closed with a vertical panel
spaced from the plate surfaces.
Inventors: |
Butt; Alan G. (La Crosse,
WI) |
Assignee: |
The Trane Company (La Crosse,
WI)
|
Family
ID: |
25359105 |
Appl.
No.: |
04/872,228 |
Filed: |
October 29, 1869 |
Current U.S.
Class: |
165/108; 165/166;
62/903 |
Current CPC
Class: |
F28D
9/0068 (20130101); F25J 3/04412 (20130101); F25J
3/04884 (20130101); F25J 5/002 (20130101); F25J
5/005 (20130101); F25J 2250/02 (20130101); F28D
2021/0033 (20130101); F25J 2290/32 (20130101); F25J
2250/20 (20130101); Y10S 62/903 (20130101) |
Current International
Class: |
F28D
9/00 (20060101); F25J 3/00 (20060101); F28g
013/06 () |
Field of
Search: |
;165/108,145,166
;29/157-3 ;62/45--55 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Matteson; Frederick L.
Assistant Examiner: Streule; Theophil W.
Claims
I claim:
1. An oxygen boiler comprising in combination: a vessel containing
a body of liquid oxygen; first means within said body of liquid
oxygen defining a first plurality of generally planar first
passages for passage of a first heat exchange fluid and each
provided with extended heat transfer fins therein; second means
within said body of liquid oxygen defining a second plurality of
generally planar substantially finless second passages for passage
of liquid oxygen and interleaved with said first passages; a
metallic heat conductive separator plate disposed between each pair
of first and second passages disposed in generally parallel
relation to a generally vertical axis for maintaining separation of
the fluids within said first and second passages and conducting
heat therebetween; said plates being of generally similar
configuration, spaced one from the other, and each having first and
second faces exposed respectively to said first and second
passages; first closing means for closing said first passages at
the edges thereof including a brazed seal extending between
adjacent faces of each of said first passages along the margins
thereof; a brazed bond between said extended heat transfer fins and
said first faces; first inlet and outlet means for passing said
first heat exchange fluid through said first passages; second inlet
and outlet means for passing liquid oxygen in said body of liquid
oxygen through a major portion of each of said second passages in a
direction generally parallel to said axis; and a second closing
means for closing said second passages at the edges thereof
including a closing panel generally parallel to said axis
traversing several of said first and second passages in overlying
relationship to said first closing means in spaced relationship to
said second faces whereby the edges of said second passages are
closed for establishing a percolator action of the liquid oxygen
within said second passages.
2. The apparatus as defined by claim 1 including a pair of side
plates each disposed at one of the opposite sides of the group of
interleaved first and second passages in generally parallel
relation to said separator plates; and means bonding vertical edges
of said closing panel to said pair of side plates.
3. The apparatus as defined by claim 1 including means bonding an
upper and a lower edge of said panel to a point on each of said
separator plates.
4. The apparatus as defined by claim 2 wherein said first inlet and
outlet means includes an inlet header and an outlet header
connected in supporting relation to said separator plates; and
means bonding upper and lower edges of said closing panel between
said inlet and outlet headers.
5. The apparatus as defined by claim 4 including means for closing
the heat exchanger side of said inlet and outlet headers in the
areas coextensive with said second passages.
6. The apparatus as defined by claim 1 where said second closing
means includes a second closing panel generally parallel to said
axis traversing several of said first and second passages in
overlying relationship to said first closing means in spaced
relationship to said second faces and disposed in remote relation
to said first mentioned closing panel.
Description
SUMMARY OF THE INVENTION
In processes involving the cryogenic separation of air it is now
common practice to use aluminum plate fin heat exchangers for
reboiling oxygen by heat exchange with warmer nitrogen gas. It is
also common practice to construct the oxygen passages free of
obstacles such as extended heat transfer surface in the form of fin
packing which is considered responsible for retention of acetylene
contaminants likely to cause dangerous explosive reactions with the
oxygen.
Plate fin heat exchangers are normally constructed by assembling
the various plate, fin and bar elements and subjecting the assembly
to a brazing furnace or bath wherein brazing metal placed at the
desired areas melts and flows within the joints of the assembly.
After the assembly is cooled, the brazing metal sealingly bonds the
various elements together.
The finless oxygen passages may be formed in a manner described in
my copending U.S. Pat. application Ser. No. 467,623 filed June 28,
1965 now U.S. Pat. No. 3,359,616 granted Dec. 26, 1967. This
application involves a method of constructing a heat exchanger with
fin packing to lend support to the assembly during the brazing
step. The fin is later pulled out to form the finless passage. In
such cases it is desirable that the faces of the oxygen passages be
kept free of braze metal, lest the pullout fin be permanently
bonded in place. However, molten braze metal in the presence of a
braze flux readily diffuses along surfaces and may flow from the
joint of the closing bar (commonly employed to form the edges of
passages) onto the heat transfer plate surfaces thereof. As
aforementioned, this is undesirable as it may prevent removal of
the pullout fin. The present invention teaches how to prevent this
braze metal diffusion onto these plate surfaces for whatever
purpose desired.
The instant invention contemplates an oxygen boiler plate-type heat
exchanger wherein the oxygen passages are free of fins and wherein
the vertical edges of the oxygen passages are closed in such a
manner as to minimize the diffusion of molten braze metal onto the
oxygen side of the heat exchanger separator plates. This is
accomplished in the instant invention by closing the edges of a
plurality of oxygen passages with a panlike panel member which is
arranged in spaced relationship with the edges of the heat transfer
plates. Since no attempt is made to provide a brazed seal in
contiguous relationship with the edges of the oxygen passages, the
problem of molten braze metal diffusion is substantially
eliminated.
It is thus a prime object of this invention to provide an oxygen
boiler heat exchanger with oxygen passages free of extended heat
transfer surface that protrudes substantially into the passage
which may cause accumulation of acetylene.
It is a further object to provide an oxygen boiler heat exchanger
which may be constructed by bulk brazing, i.e., furnace or bath
brazing, without substantial diffusion of brazing metal on the heat
transfer surfaces of the oxygen passages.
Specifically, this invention involves an oxygen boiler comprising
in combination: a vessel containing a body of liquid oxygen; first
means within said body of liquid oxygen defining a first plurality
of generally planar first passages for passage of a first heat
exchange fluid and each provided with extended heat transfer fins
therein; second means within said body of liquid oxygen defining a
second plurality of generally planar substantially finless second
passages for passage of liquid oxygen and interleaved with said
first passages; a metallic heat conductive separator plate disposed
between each pair of first and second passages disposed in
generally parallel relation to a generally vertical axis for
maintaining separation of the fluids within said first and second
passages and conducting heat therebetween; said plates being of
generally similar configuration, spaced one from the other, and
each having first and second faces exposed respectively to said
first and second passages; first closing means for closing said
first passages at the edges thereof including a brazed seal
extending between adjacent faces of each of said first passages
along the margins thereof; a brazed bond between said extended heat
transfer fins and said first faces; first inlet and outlet means
for passing said first heat exchange fluid through said first
passages; second inlet and outlet means for passing liquid oxygen
in said body of liquid oxygen through a major portion of each of
said second passages in a direction generally parallel to said
axis; and a second closing means for closing said second passages
at the edges thereof including a closing panel generally parallel
to said axis traversing several of said first and second passages
in overlying relationship to said first closing means and in spaced
relationship to said second faces whereby the edges of said second
passages are closed for establishing a percolator action of the
liquid oxygen within said second passages with a minimum number of
brazed joints at said second faces and a minimum braze metal
diffusion on said second faces.
Other objects and advantages will become apparent as this
specification proceeds to describe the invention illustrated in the
accompanying drawings wherein like elements have been designated by
like numerals throughout and in which:
FIG. 1 is a perspective of the oxygen reboiler portion of an
air-fractionating column and having portions shown in section for
viewing features of the invention;
FIG. 2 is a side elevation of one of the oxygen boiler heat
exchangers employed in the oxygen reboiler of FIG. 1;
FIG. 3 is a plan view of the heat exchanger shown in FIG. 2;
FIG. 4 is a horizontal section taken at line 4-4 in FIG. 2;
FIG. 5 is a vertical section taken at line 5-5 in FIG. 4 through
one of many similar nitrogen passages; and
FIG. 6 is a vertical section taken at line 6-6 in FIG. 4 through
one of many similar oxygen passages.
Now with reference to FIG. 1, there is shown a fractionating column
10 having a high-pressure section 12 and a low-pressure section 14.
The lower portion of low-pressure section 14 includes an oxygen
reboiler section 16 having several plate-type oxygen boiler heat
exchangers 18 circumferentially spaced and supported by lugs 20
welded or torch brazed to the vertical side plates 21 thereof and
supported on the inner side of annular wall 22 of the vessel
forming the low-pressure section. In certain of the passages of
each heat exchanger 18, oxygen is vaporized by heat from warmer
nitrogen passing through adjacent passages. An oxygen inlet conduit
24 connects the interior of the reboiler section 16 with a source
(not shown) of liquid oxygen such as oxygen rich liquid air. The
flow of oxygen rich liquid through conduit 24 may be controlled to
maintain the desired liquid level in the reboiler section with
respect to heat exchanger 18.
Nitrogen gas for vaporizing the oxygen enters the reboiler section
16 from the high-pressure section 12 via supply conduit 27 and
annular header 29 and is conducted to the heat exchangers 18 via
nitrogen inlet conduits 26. Nitrogen leaves each of heat exchangers
18 through a nitrogen outlet conduit 28 which may be connected to
return condensed nitrogen to the high-pressure section 12. The
specific structure of heat exchanger 18 is more clearly seen in
FIGS. 2--6.
Each heat exchanger 18 has a plurality of imperforate aluminum
separator plates 30 of rectangular configuration spaced in
superposed parallel relationship forming platelike or flat passages
therebetween.
Certain of these passages 32 (see FIGS. 3, 4 and 5) for nitrogen
are filled with extended heat transfer surface such as fin packing
34 for conducting heat from the nitrogen fluid to the plates 30.
Fin packing 34 may take various forms such as shown in FIGS. 9--10
of U.S. Pat. No. 3,282,334 and is oriented to provide good
distribution of the nitrogen fluid across the passage 32 from
nitrogen inlet 36 to nitrogen outlet 38. The top and bottom edge of
each passage 32 are sealingly closed by bars 40. The rear edge of
each passage 32 is sealingly closed by a bar 42 while a bar 44,
somewhat shorter than bar 42 sealingly closes the front edge of
each passage 32 and terminates short of bars 40 to form nitrogen
inlet 36 and nitrogen outlet 38. Semicylindrical headers 46 and 48
which may be welded or torch brazed to the heat exchanger core
assembly communicate the inlets 36 with inlet conduits 26 and the
outlets 38 with outlet conduits 28 respectively. Fin packing 34 and
bars 40, 42 and 44 are bulk brazed, i.e., furnace or bath braze
bonded, to the first faces 30a of plates 30 which form the
sidewalls of passages 32.
Certain other of the passages 50 (see FIGS. 3, 4 and 6) for
conducting oxygen enriched liquid are interposed between the
nitrogen passages 32. Passages 50 are constructed free of any
separate extended heat transfer surface such as the fins used in
passages 32, since fins are considered to be responsible for
acetylene accumulation which increases the risk of explosive
reactions with oxygen. The bottom and top edges of each passage 50
are completely open for circulation of oxygen.
To avoid the diffusion of braze metal on faces 30b the vertical
edges of the oxygen passages 50 are closed at the front by a
shallow generally planar panlike vertical front panel 52 disposed
between headers 46 and 48 and overlying the front edges of plates
30 and bars 44 in spaced relationship to the front edges of faces
30b of passages 50. Closing panel 52 is bonded in place along its
upper edge to header 46 and along its lower edge to header 48. The
vertical sides of panel 52 are similarly bonded to side plates 21.
The vertical edges of the oxygen passages 50 are closed at the rear
by a similar shallow panlike vertical rear panel 54 positioned to
overly the rear edges of plates 30 and bars 42 in spaced
relationship to the rear edges of faces 30b of passages 50. Closing
panel 54 is bonded in place at intervals 55 (FIG. 3) along its
upper and lower edges to bars 42 and the edge of plates 30 in the
vicinity of the ends of bars 42 thereby supporting plates 30 in
spaced relationship at their upper rear corners. The vertical sides
of panel 54 are similarly bonded to side plates 21. The heat
exchanger side of headers 46 and 48 in the areas coextensive with
passages 50 are suitably closed by a short bar member 56 which may
be similar in cross section to bars 42 and 44. These bar members 56
also support plates 30 in spaced relationship at the top and bottom
front corners. If desired, the side plates 21 may be constructed
with substantial thickness to provide the assembly with sufficient
strength.
Thus it will be seen from FIGS. 3, 4 and 6 that the front and back
edges of passages 50 are closed to promote percolator action of the
liquid fluid within passages 50. However, close clearances and wide
laps which may collect dangerous acetylene have been avoided.
During operation of the oxygen boiler, nitrogen gas which is warmer
than the liquid oxygen in reboiler section 16 is passed from
high-pressure section 12 through supply conduit 27, header 29,
through inlet conduits 26 to inlet headers 46. In each of the
passages 32 nitrogen gas enters the inlet 36 from a header 46 and
is distributed uniformly across the width of the passage whereupon
it moves downward giving up heat to bar 42, bar 44, and plates 30
partially via fin packing 34. All or part of the nitrogen may be
condensed. The nitrogen leaves passage 32 via outlet 38 which
discharges into lower header 48. Outlet conduits 28 conduct the
discharged nitrogen from headers 48 to return the same to
high-pressure section 12. The heated bars 42, 44 and plates 30
induce a percolator of the oxygen liquid within the confines of
front and rear panels 52 and 54 causing the liquid oxygen to be
swept rapidly over the bar and plate surfaces for efficient heat
transfer to the oxygen liquid. A portion of the heated liquid
oxygen is thus vaporized and may be withdrawn from the reboiler
through a conduit not shown.
Having now described in detail the preferred embodiment of my
invention, I contemplate that many changes may be made without
departing from the scope or spirit of my invention and I
accordingly desired to be limited only by the claims.
* * * * *