GB1568706A - Furnace - Google Patents
Furnace Download PDFInfo
- Publication number
- GB1568706A GB1568706A GB2251176A GB2251176A GB1568706A GB 1568706 A GB1568706 A GB 1568706A GB 2251176 A GB2251176 A GB 2251176A GB 2251176 A GB2251176 A GB 2251176A GB 1568706 A GB1568706 A GB 1568706A
- Authority
- GB
- United Kingdom
- Prior art keywords
- furnace
- pump
- venturi
- vessel
- ejector
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000012298 atmosphere Substances 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 19
- 239000012530 fluid Substances 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000002955 isolation Methods 0.000 claims description 4
- 230000005855 radiation Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 208000036366 Sensation of pressure Diseases 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 238000012423 maintenance Methods 0.000 claims description 2
- 238000012986 modification Methods 0.000 claims description 2
- 230000004048 modification Effects 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910052729 chemical element Inorganic materials 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004845 hydriding Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D7/00—Forming, maintaining or circulating atmospheres in heating chambers
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Jet Pumps And Other Pumps (AREA)
Description
(54) FURNACE
(71) We, ROLLS-ROYCE LIMITED, a
British Company, of 65 Buckingham Gate,
London SW1E 6AT, formerly ROLLS ROTcE (1971) LIMITED, a British Company,
of Norfolk House, St. James's Square,
London SW17 4JR, do hereby declare the invention, for which we pray that a patent
may be granted to us, and the method by
which it is to be performed, to be particu
larly described in and by the following statement: This invention relates to a furnace.
It is a normal requirement for furnaces
that they should have an internal tempera
ture which is substantially constant, or at
least lies within specified limits over the en
tire working area of the furnace, and in
order to achieve this in the past fans have been used to circulate the atmosphere with
in the furnace. However, such fans tend
to be bulky and require the provision of a
supply of electricity, and since they have
rotating components, it is sometimes diffi
cult to arrange that they operate satisfac
torily in special atmospheres such as for
instance as are used in hydriding furnaces.
The present invention provides a fur
nace within -which circulation of the atmos
phere is effected in a simple manner.
According to the present invention a fur nace comprises a vessel, heating means
within the vessel, a plurality of ejector
pomps mounted within the vessel, and
fluid supply means adapted to supply com
pressed fluid to the pumps, the pumps being
arranged to entrain as a secondary flow the -atmosphere within the vessel and thus to promote cirction of the atmosphere
within the vessel.
Throughout this specification the term ejector pump is to be taken to refer to
a pump within which a primary flow of
compressed fluid entrains a greater quan
tity of the same br a different fluid thus
forming a secondary flow which is the
pumped flow.
Preferaw a feed d -eoanpIe'ed gas
which is the ianie as that- mating up the
atmosphere of the vessel is supplied to the
ejector pump, and in one embodiment this
feed comprises a portion of this atmos
phere which is compressed by a separate
pump. In this case we prefer to carry the
atmosphere to a remote location where it
is cooled and compressed before returning
to the vessel to power the ejector pump.
We prefer to use the type of pump in
which flow takes place from an annulus
along the surface of a venturi, the secon
dary flow being entrained through the
venturi.
The invention will now be particularly
described, merely by way of example, with
reference to the accompanying drawings
in which: Fig. l is a schematic diagram of a fur
nace in accordance with the invention, and
Fig. 2 is a cross-section through one of
the ejector pumps used in Fig. 1.
In Fig. 1 there is shown a furnace com
prising a pressure vessel 10 within which
are mounted heating elements 11 positioned
adjacent the walls of the vessel. The ele
ments 11 in this instance are electrical re
sistance heating elements although they
could be other types as desired. A heat
shield 12 protects the major area of the
furnace from the effect of heat radiated
directly from the heating elements so that
the transfer of heat to workpieces within
the furnace is mainly effected from the hot
atmosphere of the furnace. Mounted be
tween the heat shield and the wall of the
furnace are a plurality (in this case six) of
ejector pumps 13, these pumps being pro
vided with a primary flow by way of pipes
14.
In order to provide this primary flow, the
atmosphere from the furnace, which in this
case comprises hydrogen, is removed from
the furnace through a duct 15 and flows to a heat exchanger 16. The heat exchanger
16 is provided with a flow of cooling water through passages- 17 and in the exchanger
the temperature of the hot. hydrogen is re
duced to a level at which it may be more
easily handled. From the heat exchanger
16 the gas flows through a valve 18 to a
mechanically operated pump 19. The
pump 19 may be any convenient form of
pump but in this case it comprises a pump
driven by an electric motor.
The compressed gas then passes through
a second valve 20 into a reservoir 21 which
is used to smooth out fluctuations in the
output from the pump, and it flows from
the reservoir through a regulator 22 and
filter 23 to an isolation valve 24 at which
point it connects with the pins 14. A pres
sure gauge 25 and flow meter 26 are pro
vided to monitor the pressure and flow of
the gas downstream of the filter 23.
Operation of this system is quite straight- forward in that a proportion of the furnace
atmosphere is drawn off through the pipe
15 and is cooled in the heat exchanger.
The pump raises it to a higher pressure
suitable for driving the ejector pumps 13
and the compressed gas is then returned
through the regulator, filter and isolation
valve to -drive the pumps. A number of
valves are provided to meet special condi
tions of operation; thus the valves 18 and 20
may be used to protect the pump 19 against
atmospheres within the furnace which
might otherwise damage it. For instance,
it may sometimes be necessary to evacuate
the furnace and the pump might be dam
aged by this procedure. The valve 24
enables operation of the ejector pumps to
be stopped and started at will.
Fig. 2 shows in detail the operation of
the ejector pumps themselves. The pri
mary flow of fluid enters from the pipe 14
through a connection 30 and into an annu
lar chamber 31 from where it exhausts
through an annular slot 32 formed at the
entrance of a venturi 33. The slot is ar
ranged so that it directs the gas along the
surface of the venturi, and because of the
Coanda effect the primary flow sticks to
the wall until it reaches the end of the ven
turi. In flowing through the venturi the
primary flow entrains a considerably larger
flow of secondary fluid which also flows
through the venturi as shown by the arrows
34. At the open end 35 of the venturi the primary flow detaches from the surface and together with the secondary flow discharges, at the same time entraining still more fluid which flows round the outside
of the venturi as shown by the arrows 36.
In this way the ejector pump is enabled to
move a- volume of gas which may be thirty
times as great as that of the primary flow,
although it will be appreciated that the .primary flow is at high pressure.
b will be understood that although the form of ejector pump described above is particularly convenient, there are a variety of different designs of such pumps which could be used.
It will be seen that the system described above enables even atmospheres of gases which are difficult to - handle to be circulated within the furnace by apparatus requiring very little space and very little modification to the furnace vessel itself, which may be important where this is a pressure vessel for operation at elevated or reduced pressures. Because the external pump works on cold gas it does not have such arduous conditions as it would if it were within the furnace, and it is very easily accessible for maintenance.
WHAT WE CLAIM IS: - 1. A furnace comprising a vessel, heating means within the vessel, a plurality of ejector pumps mounted within the vessel and fluid supply means adapted to supr compressed fluid to the pumps, the pumps being arranged to entrain as a secondary flow the atmosphere within the vessel and thus to promote circulation of said atmosphere.
2. A furnace as claimed in claim I and in which the motive fluid of the ejector pump comprises the same gas which makes up the atmosphere within the furnace.
3. A furnace as claimed in claim 2 and comprising a separate pump which is fed with a portion of the atmosphere within the vessel, compresses this portion and returns it through said fluid supply means to power said ejector pump.
4. A furnace as claimed in claim 3 and comprising cooling means adapted to cool said portion of the atmosphere before it is compressed by said separate pump.
5. A furnace as claimed in any preceding claim and in which each said ejector pump comprises a body within which is formed a venturi, the primary flow of the pump taking place from an annulus up stream of the venturi and the secondary flow being entrained through the venturi.
6. A furnace as claimed in any preceding claim and in which said vessel comprises heater elements spaced about its walls and a radiation shield interposed between the heater elements and the working volume, said ejector pumps being mounted between the walls and the radiation shield.
7. A furnace substantially as particularly hereinbefore described with reference to the accompanying drawings.
**WARNING** end of DESC field may overlap start of CLMS **.
Claims (7)
- **WARNING** start of CLMS field may overlap end of DESC **.easily handled. From the heat exchanger16 the gas flows through a valve 18 to a mechanically operated pump 19. The pump 19 may be any convenient form of pump but in this case it comprises a pump driven by an electric motor.The compressed gas then passes through a second valve 20 into a reservoir 21 which is used to smooth out fluctuations in the output from the pump, and it flows from the reservoir through a regulator 22 and filter 23 to an isolation valve 24 at which point it connects with the pins 14. A pres sure gauge 25 and flow meter 26 are pro vided to monitor the pressure and flow of the gas downstream of the filter 23.Operation of this system is quite straight- forward in that a proportion of the furnace atmosphere is drawn off through the pipe15 and is cooled in the heat exchanger.The pump raises it to a higher pressure suitable for driving the ejector pumps 13 and the compressed gas is then returned through the regulator, filter and isolation valve to -drive the pumps. A number of valves are provided to meet special condi tions of operation; thus the valves 18 and 20 may be used to protect the pump 19 against atmospheres within the furnace which might otherwise damage it. For instance, it may sometimes be necessary to evacuate the furnace and the pump might be dam aged by this procedure. The valve 24 enables operation of the ejector pumps to be stopped and started at will.Fig. 2 shows in detail the operation of the ejector pumps themselves. The pri mary flow of fluid enters from the pipe 14 through a connection 30 and into an annu lar chamber 31 from where it exhausts through an annular slot 32 formed at the entrance of a venturi 33. The slot is ar ranged so that it directs the gas along the surface of the venturi, and because of the Coanda effect the primary flow sticks to the wall until it reaches the end of the ven turi. In flowing through the venturi the primary flow entrains a considerably larger flow of secondary fluid which also flows through the venturi as shown by the arrows 34. At the open end 35 of the venturi the primary flow detaches from the surface and together with the secondary flow discharges, at the same time entraining still more fluid which flows round the outside of the venturi as shown by the arrows 36.In this way the ejector pump is enabled to move a- volume of gas which may be thirty times as great as that of the primary flow, although it will be appreciated that the .primary flow is at high pressure.b will be understood that although the form of ejector pump described above is particularly convenient, there are a variety of different designs of such pumps which could be used.It will be seen that the system described above enables even atmospheres of gases which are difficult to - handle to be circulated within the furnace by apparatus requiring very little space and very little modification to the furnace vessel itself, which may be important where this is a pressure vessel for operation at elevated or reduced pressures. Because the external pump works on cold gas it does not have such arduous conditions as it would if it were within the furnace, and it is very easily accessible for maintenance.WHAT WE CLAIM IS: - 1. A furnace comprising a vessel, heating means within the vessel, a plurality of ejector pumps mounted within the vessel and fluid supply means adapted to supr compressed fluid to the pumps, the pumps being arranged to entrain as a secondary flow the atmosphere within the vessel and thus to promote circulation of said atmosphere.
- 2. A furnace as claimed in claim I and in which the motive fluid of the ejector pump comprises the same gas which makes up the atmosphere within the furnace.
- 3. A furnace as claimed in claim 2 and comprising a separate pump which is fed with a portion of the atmosphere within the vessel, compresses this portion and returns it through said fluid supply means to power said ejector pump.
- 4. A furnace as claimed in claim 3 and comprising cooling means adapted to cool said portion of the atmosphere before it is compressed by said separate pump.
- 5. A furnace as claimed in any preceding claim and in which each said ejector pump comprises a body within which is formed a venturi, the primary flow of the pump taking place from an annulus up stream of the venturi and the secondary flow being entrained through the venturi.
- 6. A furnace as claimed in any preceding claim and in which said vessel comprises heater elements spaced about its walls and a radiation shield interposed between the heater elements and the working volume, said ejector pumps being mounted between the walls and the radiation shield.
- 7. A furnace substantially as particularly hereinbefore described with reference to the accompanying drawings.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2251176A GB1568706A (en) | 1977-05-27 | 1977-05-27 | Furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2251176A GB1568706A (en) | 1977-05-27 | 1977-05-27 | Furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1568706A true GB1568706A (en) | 1980-06-04 |
Family
ID=10180565
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2251176A Expired GB1568706A (en) | 1977-05-27 | 1977-05-27 | Furnace |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1568706A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4767317A (en) * | 1985-01-26 | 1988-08-30 | Carl Kramer | Apparatus for mixing a gas main flow with at least one gas subflow |
GB2329457A (en) * | 1997-09-19 | 1999-03-24 | Osaka Oxygen Ind | Generating furnace atmospheres |
-
1977
- 1977-05-27 GB GB2251176A patent/GB1568706A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4767317A (en) * | 1985-01-26 | 1988-08-30 | Carl Kramer | Apparatus for mixing a gas main flow with at least one gas subflow |
GB2329457A (en) * | 1997-09-19 | 1999-03-24 | Osaka Oxygen Ind | Generating furnace atmospheres |
GB2329457B (en) * | 1997-09-19 | 2001-03-28 | Osaka Oxygen Ind | Heat treatment atmosphere generator |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
CSNS | Application of which complete specification have been accepted and published, but patent is not sealed |