Note: Descriptions are shown in the official language in which they were submitted.
CA 02602524 2007-10-09
Specification
"Steam-Heating Apparatus"
Technical Field
This is a divisional application of Canadian Patent Application Serial No.
2,366,367 filed on Dec 15, 2000.
The present invention relates to a steam-heating apparatus in which a heating
section formed in a heat exchanger is connected with a steam supply pipe for
receiving
supply of heating steam and connected also with a condensate recovering unit
for
discharging condensate produced as a result of heating.
It should be understood that the expression "the invention" and the like
encompasses the subject-matter of both the parent and the divisional
applications.
Background Art
An example of such steam-heating apparatus is known from
Japanese paten application laid-open No. Hei. 7-328423. In this steam-
heating apparatus, as shown in Fig. 6, a reaction vessel 'i is provided as a
heat exchanger_ The reaction vessel includes, as a heating section thereof,
a jacket section 2, to which a steam supply pipe 3 for receiving supply of
heating steam and a condensate recovering un.it 6 for discharging
condensate produced as a result of heatiag are connected. More
particularly, the steam supply pipe 3 is connected to an 'inlet of a steam
ejector 5 and the jacket section 5 as a heating section is connected to a
suction chamber 13 formed in an outer periphery of a nozzle communicated
with the inlet of the steam ejector 5. - Also, a shutoff valve 47 is connected
to an outlet communicated with the suction chamber 13.
In operation, by opening the shutoff valve 47, air remaining within
the jacket section 2 vvill be drawn into the suction chamber 13 to evacuate
the inside of the jacket section 2. Thereafter, by dosi.ng the shutoff valve
47, low-pressure steam is supplied into the jacket section 2, so that an
object
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CA 02602524 2007-10-09
in the reaction vessel 1 may be heated by low-temperature steam of 100 C
or lower.
With the conventional steam-heating apparatus described above,
the apparatus is capable of steam-heating an object with the air remaining
at the initial stage of the heating process being removed by suction.
However, this apparatus cannot exhaust air which may be gxadually
accumulated wifi,h, progress of the heating process, so that the apparatus
becomes unable to maintain, a predetermined heating temperature precisely.
Specifically, when the heating apparatus is placed under the evacuated
condition below the atmospheric pressure, atmospheric air may be
inadvertently drawn through m the respective joints of the apparatus,
thus leading to gradual accumulation of air inside the heating section.
Moreover, the heating steam supplied to the apparatus may contain some
air therein. Therefore, disadvantageous accumulation of sir inside the
heating section occurs not only in the initial stage of the heating process
but
also during the subsequent heating stage thereo~
Di9closnre of the Invention
Accordingly, an object of the present invention is to provide a
steam-heating apparatus capable of adjusting the heating temperature with
high precision by effectively eliminating air which may be accumulated not
only in the initial stage of the steam-heating process but also during the
subsequent heating stage thereof.
For accomplishing the object noted above, a steam-heating
apparatus proposed by the present invention comprises a steam ejector
including a suction chamber eonnected to the heating section and an inlet
for receiving supply of heating steam, the steam ejector being actuated in
response to a drop in a temperature of the heating section by a
predetermined value so as to suck air (an example of gas) in the heating
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CA 02602524 2007-10-09
section into the suction chamber of the steam ejector.
That is, in response a drop by a predetermined value in the
temperature in e.g. the heat-ing section or in a condensate tank disposed
between this heating section and the condensate recovering device, the
steam ejector is actuated and steam is supplied to the inlet of the steam
ejector, whereby a suction force is developed in the suction chamber for
sucldng the air accumulated in the heating section therein and
subsequently exhausting this air to the outside.
Therefore, in the steam-heating apparatus, whenever the
temperature of the heating section drops by a predetermined value due to
presence of ais therein not only in the initial stage of heating, but also
during subsequent heating stage thereof, the steam ejector is actuated for
sucldng and exhausting this air.
Further, in addition to the above-described construction of the
steam-heating apparatus, the steam-heating apparatus of the invention
may further comprise a temperature-responsive valve disposed at the inlet
of the steam ejector, the temperature-responsive valve being opened in
response to the drop by the predetermined value of the temperature of the
heating section so as to supply the steam to the inlet of the steam ejector.
That is, by providing the temperature-responsive valve connected
to the inlet of the steam ejector, when air has accumulated in the heating
section to cause the temperature thereof to drop by a predetermined value,
the temperature-responsive valve is opened to introduce'steam into the inlet
of the steam ejector and the air accumulated in the heating section is
withdrawn by the resultant suction force developed in the suction chamber
to be exhausted to the outside.
In addition to the above-described constructaon of the steam-
heating apparatus, the steam-heating apparatus of the invention may
-further comprise a check valve disposed at a connection between the heating
section and the suction chamber of the steam ejector, the check valve
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allowi.ng only unidirectional passage of the air from the heating section to
the suction chamber of the steam ejector.
That is, by providing the check valve disposed between the suction
chamber of the steam ejector and the heating section or the condensate tank
in addition to the temperature-responsive valve connected to the inlet of the
steam ejector, when the temperature drops by a predetermined value as a
result of accumulation of air inside the heating section or the condensate
tank, the temperature-responsive valve is opened to supply steam to the
inlet of the steam ejector and the check valve is opened by the resultant
suction force of the steam ejector to allow communication of air from the
heating section to the suction chamber thereby to suck and exhaust the air
accumulated inside the heating section to the outside.
Further, the steam-heating apparatus of the present invention, in
addition to the above-described construction of the steam-heating apparatus,
further comprises a temperature-responsive valve disposed at a connection
between the heating section and the -suction chamber of the steam ejector,
the temperature-responsive valve being opened in response to a drop by a
predetermined value in the temperature of the heating section so as to allow
suction of the air from the heating seati.on to the suction chamber of the
steam ejector.
That is, by providing a temperature-responsive valve disposed at a
connection between the heating section and the suction chamber of the
steatn ejector, when air has accumulated inside the heating section thus
causing a drop in its temperature by a predetermined value, the
temperature-responsive valve is opened to establish communication
between the heating section and the suction chamber of the steam ejector,
whereby the air accumulated in the heating section can be sucked and
exhausted to the outside by the xesultant suction force developed in the
suction chamber.
For accomplishing the object of this invention, the steam-heating
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apparatus of the present invention comprises a condensate tank disposed
between the heating section and the condensate recovering unit and a
steam ejector having a suction chamber connected to the heating section or
to the condensate tank and an inlet for receiving supply of steam, the steam
ejector being actuated in response to a drop by a predetermined value in the
temperature inside the heating section or the condensate tank so as to suck
air in the heating section or the condensate tank into the suction chamber of
the steam ejector.
That is, when the temperature inside the heating section or the
condensate tank interposed between the heating section and the condensate
recovering unit drops by a predetermined value, the steam ejector is
actuated to cause the air in the heating section or the condensate tank to be
sucked into the suction chamber of the steam ejector. With this, when air
has accumulated inside the heating section and the condensate tank
16 resulting in a temperature drop by a predetermined value, the steam ejector
is actuated so that steam is supplied to the inlet of the steam ejector from
e.g. a steam supply pipe an the resultant suction force developed in the
suction chamber can suck the air accumulated inside the heating section
and the condensate tank and exhaust the air to the outside.
Accordingly, in the steam-heating apparatus, both in the initial
stage of heating and during the subsequent heating stage, whenever air has
accumulated inside the heating section or the condensate tank thus
resulting in such temperature drop, the steam ejector is actuated to suck
and exhaust the air.
Further, the steam-heating apparatus of this invention, in addition
to the above-described construction of the steam-heating apparatus, further
comprises a temperature-resporisive valve disposed at the inlet of the steam
ejector, the temperature-responsive valve being opened in response to a
drop by 'a predetermined value in the temperature inside the heating
section or the condensate tank so as to supply the steam of the steam supply
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pipe to the inlet of the steam ejector.
That is to say, in case the steam-heating apparatus includes a
condensate tank, there is provided the temperature-responsive valve
connected to the inlet of the steam ejector. With this, when air has
accumulated inside the heating section or the condensate tank resulting in a
temperature drop by a predetermined value, the temperature-responsive
valve is opened so as to supply steam to the inlet of the steam ejector and a
suction force is developed in the suction chamber. With this, the air
accumulated in the heating section and the condensate tank may be sucked
into the suction chamber via a check valve or the like provided between the
suction cbamber of the steam ejector and the condensate tank and the air
may be exhausted to the outside subsequently.
Further, the steam-heating apparatus of the present invention, in
addition to the above-described constructiou of the steam-heating apparatus,
further comprises a check valve provided at a eonnection between the
heating section or the condensate tank and the suction chamber of the
steam ejector, the check valve allowing only unidirectional gas passage from
the heating section or the condensate tank to the suction chamber of the
steam ejector.
That is, by providing a check valve between the suction chamber of
the steam ejector and the heating section or the condensate tank in addition
to the temperature-responsive valve connected to the inlet of the steam
ejector, when air has accumulated inside the heating section or the
condensate tank thus xesulting in a drop in its temperature by a
predetermined value, the temperature-responsive valve is opened to supply
steam to the inlet of the steam ejector and the check valve is opened by the
resultant suction force from the steam ejector so as to allow communication
of air from the heating section or the condensate tank to the suction
chamber, so that the air accumulated inside the heating section or the
condensate tank may be sucked and exhausted to the outside by the suction
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force in the suction chamber.
For accomplishuig the object of this invention, with the steam-
heating apparatus of the present invention, the condensate recovering unit
includes a high-pressure control fluid inlet for receiving supply of high-
pressure control fluid for pressure-transporting and discharging the
conderasate, the apparatus comprises an ejector including a suction chamber
connected to the heating section, an inlet for receivin.g supply of the high-
pressure control fluid and an outlet connected to the high-pressure control
fluid inlet and further comprises a valve means provided at a connection
between the heating section and the suction chamber of the steam ejector.
That is to say, the ejector is incorporated in a high-pressure control
fluid passage for passing the high-pressure control fluid; the outlet of the
ejector is connected to the high-pressure control fluid inlet of the
condensate
recovering unit; and the suction chamber of the ejector and the heating
sectaon are connected to each other via the valve means comprising e.g. a
shutoff valve. In operation, when the high-pressure control fluid is
introduced into the condensate recovering unit thereby to pass the high-
pressure control fluid through the ejector, a suction force is developed in
the
suction chamber of the ejector, whereby air accumulated inside the heating
section may by sucked and exhausted via the valve means.
Accordingly, both in the iu.itial stage of the heating and the
subsequent heati-ag stage, each time the high-pressure control fluid is
introduced into the condensate recovering unit, a suction force is developed
in the ejector, so that the air accumulated in the heating section may be
eliminated.
For accomplishing the object of this. invention, with the steam-
heating apparatus of the present invention, the condensate recovering unit
includes a high-pressure control fluid inlet for receiv3ng supply of high-
pressure control fluid for pressure-transpoxting and exhausting the
condensate and a condensate returning outlet for exhausting the pressure-
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transported condensate, the apparatus comprises an ejector including a
suction chamber connected to the heating section and an inlet connected to
the condensate returning outlet, and the etpparatus further comprises a
valve means provided at a connection between the heating section and the
suction chamber of the steam ejector.
That is to say, the ejector is incorporated in a high-pressure control
fluid passage connected to the condensate returning outlet of the condensate
recovering unit and the suction chamber of the ejector and the heating
section are connected to each other via the valve means comprising e.g. a
shutoff valve, In operation, when the high-pressure control fluid is '
introduced from the condensate pressure-transporting passage thereby to
pass the condensate through the ejector, a suction force is developed in the
suction chamber of the ejector, whereby air accumulated inside the heating
section may by sucked and exhausted via the valve means.
During both the initial stage of the heating process and the
subsequent heating stage of the same, a suction force is developed in the
ejector every time the condensate is pressure-transported from the
condensate pressure-transporting passage of the condensate recovering unit,
whereby air a,ccumulated inside the heatang section may be sucked and
exhausted
Further, with the steam-heating apparatus of the present
invention, in addition to the above-described construction, the valve means
comprises a temperature-responsive valve which is opened in response to a
drop in the temperature by a predetermined value in the heating section or
between the heating section or the condensate recovering unit so as to aIlow
suction of air from the heating section into the suction chamber of the
ejector.
That is to say, when the temperature in the heating section or
between the heating section and the condensate xecoveri.ng unit, such as in
the condensate tank, drops by a predetermined value, the temperature-
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responsive valve as the.valve means is opened to establish communication
between the heating section and the suction chamber of the steam ejector,
so that the resultant suction force developed in the suction chamber sucks
and exhausts the air accumulated inside tlte heating section to the outside.
According to an aspect of the present invention there is provided a stream-
heating
apparatus in which a heating section formed in a heat exchanger is connected
to a stream
supply pipe for receiving supply of heating steam and connected also to a
condensate
recovering unit for discharging produced as a result of heating, the apparatus
comprising:
a steam ejector including a suction chamber connected to the heating section
and an
inlet for receiving supply of the steam;
wherein the steam ejector is actuated in response to a drop in the temperature
of the
heating section by a predetermined value to cause gas in the heating section
to be sucked
into the suction chamber of the steam ejector.
According to'another aspect of the present invention there is provided a steam-
heating apparatus in which a heating section formed in a heat exchanger is
connected to a
steam supply pipe for receiving supply of heating steam and connected also to
a
condensate recovering unit for discharging condensate produced as a result of
heating,
the apparatus comprising:
a condensate tank disposed between the heating section and the condensate
recovering
unit;
a steam ejector including a suction chamber connected to the heating section
or to the
condensate tank and an inlet for receiving supply of steam:
a temperature sensor mounted to a portion of the heating section or the
condensate tank, for detecting temperature of the heating section or the
condensate tank;
a means for operating the steam ejector based on the temperature detected by
the
temperature sensor; and
wherein said operating means actuate the steam ejector in response to a drop
in
the temperature of the heating section or in the condensate tank by a
predetermined value
to cause gas in the heating section or in the condensate tank to be sucked
into the suction
chamber of the steam ejector.
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According to an aspect of the present invention there is provided a steam-
heating
apparatus in which a heating section formed in a heat exchanger vessel is
connected to a
steam containing control fluid supply pipe for receiving supply of steam
containing high-
pressure control fluid and is connected also to a condensate recovering unit
for collecting
condensate from the heating section produced as a result of heating the heat
exchange
vessel,
wherein said condensate recovering unit includes a high-pressure control fluid
inlet for
receiving high-pressure control fluid for pressure-transporting and
discharging the
condensate; and
the apparatus further comprises:
an ejector including a suction chamber connected to the heating section for
evacuating
the heating section, said ejector having an inlet for receiving supply of the
high-pressure
control fluid and an outlet connected to the high-pressure control fluid inlet
of the
condensate unit, and
a valve means for connecting the heating section and the suction chamber of
the ejector
when air has accumulated in the heating section.
According to another aspect of the present invention there is provided a steam-
heating apparatus in which a heating section formed in a heat exchanger vessel
is
connected to a steam containing control fluid supply pipe for receiving supply
of steam
containing high-pressure control fluid and is connected also to a condensate
recovering
unit for collecting condensate from the heating section produced as a result
of heating the
heat exchange vessel,
wherein said condensate recovering unit includes a high-pressure control fluid
inlet for
receiving high-pressure control fluid for pressure-transporting and
discharging the
condensate; and
the apparatus further comprises:
an ejector including a suction chamber connected to the heating section for
evacuating
the heating section, said ejector having an inlet for receiving supply of the
high-pressure
control fluid and an outlet connected to the high-pressure control fluid inlet
of the
condensate unit, and
a valve means for connecting the heating section and the suction chamber of
the ejector
when air has accumulated in the heating section.
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According to another aspect of the present invention there is provided a steam-
heating apparatus in which a heating section formed in a heat exchanger vessel
is
connected to a steam containing control fluid supply pipe for receiving supply
of steam
containing high-pressure control fluid and is connected also to a condensate
recovering
unit for collecting condensate from the heating section produced as a result
of heating the
heat exchange vessel,
wherein said condensate recovering unit includes a high-pressure control fluid
inlet for
receiving high-pressure control fluid for pressure-transporting and exhausting
the
condensate and a condensate returning outlet for exhausting the pressure-
transported
condensate; and
the apparatus comprises:
an ejector including a suction chamber connected to the heating section for
evacuating the heating section, said ejector having an inlet connected to the
condensate
returning outlet of the condensate unit, and
a valve means for connecting the heating section and the suction chamber of
the ejector
when air has accumulated in the heating section.
Brief Description of the Drawings
Fig_ 1 is a constructioia view sbowing a first mode of embodiment of
a steam-heating apparatus according to the present invention,
Fig. 2 is a construction view showing a second mode af embodiment
of a steam-heating apparatus according to the present invention,
Ilg. 3 is a construction view showi.ng a third mode of embodiment
of a steam-heating apparatus aocorcling to the present invention,
Fig. 4 is a construction view showing a fourth mode of embodiment
of a steam-heating apparatus according to the present invention,
Fig. 5 is a construction view showing a fifth mode of embodiment of
a steam-heating apparatus according to the present invention, and
Fig. 6 is a constructaon view showing a steam-heating apparatus
according to the prior art.
9b
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S I
Best Mode of Embodying the Invention
(first mode of embodiment)
A first mode of embodiment of a steam-heating apparatus will be
described with reference to Fig. 1 in which a reaction vessel 1 is employed as
a heat exchanger.
In the steam-heating apparatus shown in Fig. 1, a jacket section 2
formed as a heating section in the outer periphery of the reaction vessel 1 is
connected to a steam supply pipe 3. Further, the apparatus includes a
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~ 4 =
temperature-responsive valve 12 connected to a branch steam supply pipe 4
and a condensate recovering unit 6 disposed downwardly of the jacket
section 2.
The steam supply pipe 3 incorporates a pressure control valve 7
and a shutoff valve 8 and is connected to the jacket section 2. The pressure
control valve 7 sets the pressure of steam to be supplied to the jacket
section
2 so that its temperature becomes a predetermined value. Further, the
steam supply pipe 3 is connected via a pipe line 9 to a high-pressure control
fluid inlet 10 of the condensate recovering unit 6.
The branch steam supply pipe 4 is connected via a shutoff valve 11
and the temperature-responsive valve 12 to an inlet of a steam ejector 5.
The steam ejector 5 includes a suction chamber 13 which is comxnunicated
with the jacket section 2 via a pipe li.n.e 15 incorporating a check valve 14
therein. This check valve 14 allows only unidirectional passage of fluid
from the jacket section 2 to the suction chamber 13, not allowing fluid
passage in. the reverse direction. .An, outlet of the steana. ejector 5 is
connected to a pipe line 16 to be communicated with a separately provided
steam-using portion not shown.
In this embodiment, the temperature-responsive valve 12 is
constructed as a self-actuated temperature control valve including a
teamperature-responsive cylinder 17 mounted to a portion of the jacket
section 2 where accumulation of air tends to occur and an actuator portion
18 of the temperature-responsive valve 12, the cylinder 17 and the actuator
portion 18 being connected to each other via a flexible tube 19. That is, the
temperature-responsive valve 12 is opened when the temperature-
responsive cylinder 17 detects a drop in the temperature inside the jacket
section 2. More particularly, when the temperature inside the jacket
section 2 drops, this results in reduction in the volume of a temperature-
responsive fluid contained in the temperature-responsive cylinder 17, which
reduction in turn results in pressure reduction in the temperature-
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,+ .
responsive fluid due to its volume reduction. Then, the developed pressure
reduction is transmitted via the flexible tube 19 to the actuator portion 18,
whereby the temperature-responsive valve 12 is opened. Conversely, when
the temperature inside the jacket section 2 rises, this temperature rise is
detected by the temperature-responsive cylinder 17, whereby the
temperature-responsive valve 12 is dosed.
As described above, with the temperature-responsive valve 12
provided at the connection between the steam supply pipe 4 and the inlet of
the ejector 5 and the check valve 14 provided at the connection between the
jacket section 2 and the suction chamber 13 of the steam ejector 5, when air
is accuznulated" inside the jacket section 2 thereby to develop a
corresponding drop in the temperature by a predetermined value, steam is
supplied to the steam ejector 5, so that the resultant suction force developed
in the suction chamber 13 sucks the air accumulated inside the jacket
section 2 and exhausts this air to the outside.
A lower portion of the jacket section 2 is connected with a
condensate inlet 20 of the condensate recovering unit 6 via a pipe line 21
which incorporates therein a valve 22 and a check valve 23. The check
valve 23 allows only unidirectional passage of fluid from the jacket section 2
to the condensate recovering unit 6, not allowing fluid passage in the
reverse direction. A condensate pressure-transporting pipe 26 is attached
also via a check valve 25 to a condensate returning outlet 24 of the
condensate recovering unit 6. This check valve 25 allows only
unidirectional fluid passage from the condensate recovering unit 6 to the
condensate pressure-transporting pipe 26, not allowing fluid passage in the
reverse direction.
The condensate recovering unit 6 further includes an exhaust
returning outlet 27 for the high-pressure control flwid disposed at the upper
portion of the unit beside the high-pressure control fluid inlet 10, and this
exhaust returning outlet 27 is connected to a pipe line 28, which in turn is
11
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, = . .
connected to an unillustrated header or any other portion which has a lower
pressure than another jacket section 2 provided separately.
When an unillustrated float contained in the unit 6 is located at a
lower position, the condensate recovering unit 6 closes the high-pressure
control fluid inlet 10 and also opens the exhaust returning outlet 27,
whereby condensate inside the jacket section 2 is caused to flow down into
the recovering unit 6 via the pipe line 21, the check valve 23 and the
condensate inlet 20. Then, when the condensate is gradually accumulated
within the recovering unit 6 to push up the float to a predetermined upper
position, the unit doses the exhaust returning outlet 27 and opens the high-
pressure control fluid inlet 10, whereby high-pressure steam as a high-
pressure control fluid is allowed into the condensate recovering unit 6 via
the steam supply pipe 3 and the condensate inside the unit is pressure-
transported via the condensate returning outlet 24, the check valve 25 and
the pipe line 26 to a condensate recovering area, where the condensate is
recovered.
When the water level inside the recovering unit 6 is lowered as a
result of recovery of the condensate, the high-pressure control fluid inlet 10
is again dosed and the exhaust returning outlet 27 is opened, whereby the
condensate is caused to flow down into the recovering unit 6 via the
condensate inlet 20. With repetition of such operational cycle, the
condensate recovering unit 6 can recover the condensate produced inside
the jacket section 2.
In p'ig. 1, when an object is to be heated inside the reaction vessel 1,
first, steam i-a the steam supply pipe 3 is supplied via the pressure control
valve 7 to the jacket section 2. Inside this jacket section 2, a certain
amount of air remains initiall,y, because of which the temperature thereof
has been dropped. Accordingly, the temperature-responsive valve 12 is
opened so as to supply the steam from the steam supply pipe 4 to the steam
ejector 5. With this, there is developed a suction force inside the suction
12
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, . r
chamber 13 of the steam ejector 5, which suction force then sucks the
remaining air of the jacket section 2 into the suction chamber 13 via the
check valve 14 and exhausts this air to the outside. When the temperature
inside the jacket section 2 reaches a predetermined value, the temperature-
responsive valve 12 is dosed to stop the suction, whereby the steam is
supplied via the pressure control valve 7 to the jacket section 2 thereby to
heat the reaction vessel 1.
After heating the reaction vessel 1, the steam is rendered into
condensate, which flows through the pipe line 21 down into the condensate
recovering unit 6_ By supplying the heating steam having a
predetermined pressure, i.e. a predetermi.iaed temperature, into the jacket
section 2 from which the air has been eliminated, the reaction unit 1 is
heated by the steam of the predetei-mined temperature. For instance,
when steam having a pressure below the atmospheric pressure and 609C is
16 supplied via the pressure control valve 7, the reaction vessel 1 is heated
at
609C.
When the inside of the jacket section 2 is set at such pressure below
the atmospheric pressure, the atmospheric pressure may act on the
respective connections, so that a portion of atmospheric air may enter the
jacket section 2 and this air or air mixed in the supplied steam may cause
accunlulation of air inside the jacket section 2, whereby the. temperature of
the jacket section 2 may be reduced due to heat discharge. Then, this
temperature drop is detected by the temperature-responsive cylinder 17 to
open the temperature-responsive valve 12, whereby steam is supplied from
the steam supply pipe 4 into the steam ejector 5 and a suction force is
developed in the suction chamber 13 of the steam ejector 5. As a result, the
air remaining in the jacket section 2 is sucked via the check valve 14 into
the suction chamber. 13 and exhausted to the outside. In this way,
according to the present embodiment, not only air present in the initial state
of the steam-heating apparatus but also air accumulated during the
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, . =
subsequent heating process may be sucked and exhausted to the outside by
the steam ejector 5.
The steam having heated the reaction vessel 1 is condensed and
rendered into the condensate, whereby its specific volume is reduced
significantly, so that the inside of the jacket section 2 is maintained at the
initial pressure condition. On the other hand, the condensed condensate
flows down into the condensate recovering unit 6. And, with repetition of
the operations described above, the condensate is pressure-txansported to
the condensate recovering portion.
(second mode of embodiment)
A second mode of embodiment of a steam-heating apparatus will be
described with reference to Fig. 2 in which a reaction vessel 1 is employed as
a heat exchanger.
In the following discussion, the same construction as that of the
foregoing embodiment will be omitted.
In the steam-heating apparatus shown in Fig. 2, a jacket section 2
formed as a heating section in the outer periphery of the reaction vessell is
connected to a stearrx supply pipe 3. Further, the apparatus indudes a
steam ejector 5 connected to a branch steam supply pipe 4, a temperature-
responsive valve 12 provided a connection between a suction chamber 13 of
the steam ejector 5 and the jacket section 2 and includes also a condensate
recovering unit 6 disposed downwardly of the jacket section 2.
That is, the branch steam supply pipe 4 is connected via a shutoff
valve 11 to an inlet of a steam ejector 5. The suction chamber 13 of the
steam ejector 5 and the jacket section 2 are communicated with each other
via a pipe line 15 incorporating a shutoff valve 29 and the temperature-
responsive valve 12. An outlet of the steam ejector 5 is connected to a pipe
line 16 to be communicated with a separately provided steam-using
14
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portion not shown.
In this embodiment, like the foregoing embodiment, the
temperature-responsive valve 12 is constructed as a self-actuated
temperature control valve.
As described above, with the temperature-responsive valve 12
provided at the connection between the jacket section 2 and the suction
chamber 13 of the steam ejector 5 and the shutoff valve 11 for supplying
steam to the steam ejector 5, when air is accumulated inside the jacket
section 2 thereby to develop a corresponding drop in the temperature by a
predetermined value, steam is supplied to the steam ejector 6, so that the
resultant suction force developed in the suction chamber 13 sucks the air
accumulated inside the jacket section 2 and exhausts this air to the outside.
In Fig. 2, when an object is to be heated inside the reaction vessel 1,
first, =steam in the steam supply pipe 3 is supplied via the pressure control
valve 7 to the jacket section 2. Inside this jacket section 2, a certain
amount of air remains initially, because of which the temperature thereof
has been dropped. Accordingly, the temperature-responsive valve 12 is
opened so as to establish communicatian between the suction chamber 13 of
the steam ejector 6 and the jacket section 2 so that the air remaining inside
the jacket section 2 is sucked into the suction chamber 13 to be exhausted to
the outside. When the temperature inside the jacket section 2 reaches a
predetermined value, the temperature-respousive valve 12 is dosed to stop
the sucdon, whereby the steam is supplied via the pressure control valve 7
to the jacket section 2 thereby to heat the reaction vessel 1. Incidentally,
it
is conceivable to adapt the pressure control valve 7 to be normally open so as
to supply steam to the steam ejector 5. Instead, it is also conceivable to
arrange that the valve is opened/dosed i.n operative association with the
temperature-responsive valve 12, whereby the valve is opened only when
the air remaining in the jacket section 2 is to be sucked into the suction
chamber 13.
CA 02602524 2007-10-09
When the inside of the jacket section 2 is set at such pressure below
the atmospheric pressure, the atmospheric pressure may act on the
respective connections, so that a portion of atmospheric air may enter the
jacket section 2 and this air or air mixed in the supplied steam may cause
accumulation of air inside the jacket section 2, whereby the temperature of
the jacket section 2 may be reduced due to heat discharge. Then, this
temperature drop is detected by the temperature-responsive cylinder 17 to
open the temperature-responsive valve 12, whereby communication is
establi.ghed between the suction chamber 13 of the steam ejector 5 and the
jacket section 2. As a result, the air remaining in the jacket section 2 is
sucked into the suction chamber 13 and exhausted to the outside. In this
way, accordang to the present embodiment, not only air present in the initial
state of the steam-heating apparatus but also air accumulated during the
subsequent heating process may be sucked and exhausted to the outside by
the steam ejector 5.
In the steam-heating apparatus of both the first and second modes
of embodiment, the steam supply pipe 4 for supplying steam to the inlet of
the steam ejector 5 is connected to a portion of the steam supply pipe 3 for
supplying steam to the inlet of the steam ejector 5 downstxeam of the
pressure control valve 7. Alternatively, the steam supply pipe 4 may be
connected to a portion -upstream of the pressure control valve 7. In such
case, it is possible to supply to the steam ejector 5 a high-pressure steam
prior to its pressure adjustanent. Still alternatively, in the steam-heating
apparatus of the invention, the steam supply pipe 4 may be provided
separately from the steam supply pipe 3, so that steam is supplied
separately to the respective steam supply pipes 3, 4.
(third mode of embodiment)
A third mode of embodiment of asteam-heating apparatus wi71 be
16
CA 02602524 2007-10-09
. ~- described with reference to Fig. 3 in which a reaction vessel 1 is
employed as
a heat exchanger.
In the following discussion, the same construction as that of the
foregoing embodiment will be omitted.
In the steam-heating apparatus shown in Fig. 3, a jacket section 2
formed as a heating section in the outer periphery of the reaction vessel 1 is
connected to a steam supply pipe 3. Further, the apparatus includes a
temperature-responsive valve 12 connected to a branch steam supply pipe 4,
a steam ejector 5, a condensate tank 110 disposed downwardly of the jacket
section 2 and a condensate recovering unit 6.
The steam supply pipe 3 incorporates a pressure control valve 7 for
setting the pressure of steam to be supplied to the jacket section 2 so that
its
temperature becomes a predetermined value. And, this pipe 3 is connected
to the jacket section 2. Further, the steam supply pipe 3 is connected via a
pipe line 9 branched from the branch steam supply pipe 4 to a high-pressure
control fluid inlet 10 of the condensate recovering unit 6.
The branch steam supply pipe 4 is connected via the pressure-
responsive valve 12 to atn inlet of the steam ejector 5. A suction.chamber 13
of the steam ejector 5 and an upper portion of the condensate tank 110 are
communicated with each other via a check valve 14. This check valve 14
allows only unidirectional fluid passage from the condensate tank 110 to the
suction chamber 13, not allowing fluid passage in the reverse direction. An
outlet of the steam ejector 5 is connected to a pipe line 16 and communicated
with a condensate pressure-transporting pipe line 26 described later.
Zn this embodiment, like the foregoing embodiments, the
temperature-responsive valve 12 is constructed as a self-actuated
temperature control valve. However, the temperature-responsive cylinder
17 of this temperature-responsive valve 12 is mounted to a portion of the
condensate tank 110 where air tends to be accumulated: That is, the
temperature-responsive valve 12 is opened when the temperature-
17
CA 02602524 2007-10-09
, .. .
responsive cylindex 17 detects a temperature drop inside the condensate
tank 110. As described above, with the temperature-responsive valve 12
provided at the connection between the steam supply pipe 4 and the iril,et of
the ejector 5 and the check valve 14 provided at the connection between the
condensate tank 110 and the suction chamber 13 of the steam ejector 5,
when air is accumulated inside the condensate tank 110 thereby to develop a
corresponding drop in the temperature by a predetermined value, steam is
supplied to the steam ejector 5, so that the resultant suction force developed
in the suction chamber 13 sucks the air accumulated inside the condensate
tank 110 and the jacket section 2 and exhausts this air to the outside.
In this embodiment, the temperature-responsive cylinder 17 of the
temperature-responsive valve 12 is attached to the upper portion of the
condensate tank 110. Instead, the temperature-responsive cylinder 17 may
also be attached to an upper or lower portion of the jacket section 2 or nlay
even be mounted inside the reaction vessel 1.
The lower portion of the jacket section 2 and a lateral portion of the
condensate tank 110 are connected by a pipe line 21 via a valve 22. Further,
the lower portion of the condensate tank 110 and the condensate inlet 20 of
the condensate recovering unit 6 are connected by a pipe line 8 via a check
valve 23. This check valve 23 allows only unidirectional fluid passage from
the condensate tank 110 to the condensate recovering unit 6, not allowing
fluid passage in the reverse direction. A condensate pressure-transporting
pipe 26 is attached also via a check valve 25 to a condensate returiu-ag
outlet
24 of the condensate recovering unit 6. This check valve 25 allows only
uniduectional fluid passage from the condensate recovering unit 6 to the
condensate pressure-transporting pipe 26, not allowing fluid passage in the
reverse direction.
The condensate recovering unit 6 further includes an exhaust
returning outlet 27 for the high-pressure control fluid disposed at the upper
18
CA 02602524 2007-10-09
, .. .
portion of the unit beside the high-pressure control fluid inlet 10, and this
exhaust returning outlet 27 is connected to a pipe line 28, which in turn is
connected to the inside of the condensate tank 110 vtirhich has a
substantially
same pressure as the jacket section 2.
When an unillustrated float contained in the unit 6 is located at a
lower position, the condensate recovering unit 6 doses the high-pressure
control fluid inlet 10 and also opens the -exhaust returning outlet 27,
whereby condensate inside the condensate tank 110 is caused to flow down
into the recovering unit 6 via the pipe line 8, the check valve 23 and the
condensate inlet 20. Then, when the condensate is gradually accumulated
within the recovering unit 6 to push up the float to a predetermined upper
position, the unit doses the exhaust returning outlet 27 and opens the high-
pressure control fluid inlet 10, whereby high-pressure steam as a high-
pressure control fluid is allowed into the unit 6 via the steam supply pipe 3
and the condensate inside the unit is pressure-transported via the
condensate returning outlet 24, the check valve 25 and the pipe line 26 to a
condensate recovering area, where the condensate is recovered.
When the water level inside the recovering unit 6 is lowered as a
result of recovery of the condensate, the high-pressure control fluid inlet 10
is again closed and the exhaust returning outlet 27 is opened, whereby the
condensate is caused to flow down into the, recovering unit 6 via the
condensate. inlet 20. With repetition of such operational cycle, the
condensate recovering unit 6 ean recover the condensate produced inside
the jacket section 2 via the condensate tank 110.
In Fig. 3, when an object is to be heated inside the reaction vessel 1,
first, steam in the steam supply pipe 3 is supplied via the pressure control
valve 7 to the jacket section 2. Inside this jacket section 2, a certain
amount of air remains irnitaa]ly and also air has entered also from the jacket
section 2 as being pushed by the steam, because of which the temperature
'30 thereof has been dropped. Accordingly, the temperature-responsive valve
19
CA 02602524 2007-10-09
, .. .
12 is opened so as to establish communication between suction chamber 13
of the steam ejector 5 and the condensate tank110, so that the air remaining
in the condensate tank 110 is sucked via the check valve 14 into the suction
chamber 13 of the steam ejector 5 and exhausted to the outside. When the
temperature inside the condensate tank 110 and subsequently the
temperature inside the jacket section 2 reaches a predetermined value, the
temperature-responsive valve 12 is closed to stop the suction, and on the
other hand, the steam is supplied via the pressure control valve 7 to the
jacket section 2 thereby to heat the reaction vessel 1.
After heating the reaction vessel- 1, the steam is condensed and
rendered into condensate, which flows through the pipe line 21 down into
the condensate recovering unit 6 from the condensate tank 1. The pressure
and the temperature of saturated steam have one-to-one relationship.
Hence, by supplying the heating steam having a predeterininedpressure, i.e.
a predetermined temperature into the jacket section 2 from which the air
has been eliminated, the reaction unit 1 is heated by the steam of the
predetermined temperature. For instance, when steam having a pressure
below the atmospheric pressure and 609C is supplied via the pressure
control valve 7, the reaction vessel I is heated at 60 C.
When the inside of the jacket section 2 is set at such pressure below
the atmospheric pressure, the atmospheric pressure may act on the
respective connections, so that a portion of atmospheric air may enter the
jacket section 2 and this aix ox air zrlixed in the supplied steam may cause
accumulation of air inside the jacket section 2 and consequently inside the
condensate tank 110 as well, whereby the temperature is reduced due to heat
discharge by 5 to 109C from the saturation temperature. Then, this
temperature drop is detected by the temperature-responsive cylinder 17 to
open the temperature-responsive valve 12, whereby steam is supplied from
the steam supply pipe 4 into the steam ejector 6 and a suction force is
developed in the suction chamber 13 of the steam ejector 5. As a result, the
CA 02602524 2007-10-09
~ ! Y
air remaining in the condensate tank 110 is sucked via the check valve 14
into the suction chamber 13 and exhausted to the outside. In this way,
according to the present embodiment, not only air present in the initial state
of the steam-heatiug apparatus but also air accumulated during the
subsequent heating process may be sucked and exhausted to the outside by .
the stea.m ejector 5.
The steam having heated the reaction vessel 1 is condensed and
rendered into the condensate, whereby its specific volume is reduced
significantly, so that the inside of the jacket section 2 is maintained at the
initial pressure condition. On the other hand, the condensed condensate
flows down fxom the condensate tank 110 into the condensate recovering unit
6. And, with repetition of the operations described above, the condensate is
pressure-transported to the condensate recovering portion.
As described in the present embodiment, as the temperature-
responsive valve 12 is opened/closed with deteciaon of the temperature of
the condensate tank i 10, it becomes possible to provide the temperature-
responsive valve 12, the ejector 5, the condensate tank 110_ and the
condensate recovering unit 6 as one integral unit. Then, by attaching this
unit to a hot-water heating apparatus such as an existing reaction vessel 1
for replacement, the apparatus may be readily converted into a steam-
heating apparatus.
(fourth mode of embodiment)
A fourth mode of embodiment of a steam-heating apparatus will be
described with reference to Fig. 4 in which a reaction vessel 1 is employed as
a heat exchanger.
In the following discussion, the same construction as that of the
foregoing embodiments will. be omitted.
In the steam-heating apparatus shown in Fig. 4, a jacket section 2
21
CA 02602524 2007-10-09
r =. r
formed as a heating section in the outer periphery of the reaction vessel 1 is
connected to a steam supply pipe 3. Further, the steam supply pipe 3 is
connected via a pipe line 9 to a high-pressure control fluid inlet 10 of a
condensate recovering unit 6. The pipe line 9 incorporates an ejector 5 and
a suction chamber 13 of the ejector 5 and the jacket section 2 are connected
with each other via a pipe line 15.
The steam supply pipe 3 incorporates a pressure control valve 7 for
setting the pressure of steam to be supplied to the jacket section 2 so that
its
temperature becomes a predeterminned value. And, this pipe 3 is connected
to the jacket section 2.
The branch pipe line 9 is connected via a shutoff valve 4 to the
ejector 5. An outlet of the ejector 6 is connected to a high-pressure control
fluid inlet 10 of the condensate recoveri.ng unit 6. The suction chamber 13
of the ejector 5 and the jacket section 2 are communicated by a pipe Iine 15
via a shutoff valve 29 and a temperature-responsive valve 12. In this
embodiment, the shutoff valve 29 and the temperature-responsive valve 12
together co .stitute a valve means.
In this embodiment, like the foregoing embodiments, the
temperature-responsive valve 12 is constructed as a self-actuated
temperature control valve including a temperature-responsive cylinder 17
mounted to a portion of the jacket section 2 where accumulation of air tends
to occur and an actuator portion 18 of the temperature-responsive valve 12,
the cylinder 17 and the actuator portion 18 being connected to each other
via a flexible tube 19.
Like the foregoing embodiments, the condensate recovering unit 6
closes the high-pressure control fluid inlet 10 and also opens the exhaust
returning outlet 27 when an uuiillustrated float contained in the unit 6 is
located at a lovwer position, whereby condensate inside the jacket section 2
is
caused to flow down into the recovering unit 6 via the pipe line 2 7, the
check
valve 23 and the condensate inlet 20. Then, when the condensate is
22
CA 02602524 2007-10-09
. .r .
gradually accumulated within the recovering unit 6 to push up the float to a
predetermined upper position, the unit closes the exhaust returning outlet
27 and opens the high-pressure control fluid inlet 10, whereby high-
pressure steam as a high-pressure control fluid is allowed into the unit 6 via
the steam supply pipe 3 and the condensate contained therein is pressure-
transported via the condensate returning outlet 24, the check valve 25 and
the pipe line 26 to a corfdensate recovering area, where the condensate is
recovered.
And, each time the high-pressure steam as a high-pressure control
fluid is supplied from the inlet 10 into the condeneate recovering unit 6, the
high-pressure steam is caused to pass also the ejector 5, whereby a suction
force can be developed in the suction chamber 13. Also, when the inlet 10
is closed, the high-pressure steam is not caused to pass the ejector 5, so
that
no suction force is developed, either.
In Fig. 4, when an object is to be heated inside the reaction vessel 1,
first, steam in the steam supply pipe 3 is supplied via the pressure control
valve 7 to the jacket section 2. In the case of this embodiment, since the
pipe line 15 includes a branch pipe 112 and a shutoff valve 16, the remaining
air initially present inside the jacket section 2 may be exhausted by opening
the shutoff valve 16. That is to say, by supplying steam via the pressure
control valve 7 to.the jacket section 2 and also opening the shutoff valve 16,
the air reinaining inside the jacket section 2 is forced out by means of the
steam.
Further, when some air rezuaine inside the jacket section 2, the
temperature inside the jacket section 2 has dropped. Hence, the
temperature-responsive valve 12 is opened so as to establish communication
between suction chamber 13 of the steam ejector 5 and the jacket section 2.
So that, with each development of suction force inside the suction chamber
13 of the ejector 5, the remaining air inside the jacket section 2 is sucked
and exhausted to the outside. When the temperature inside the jacket
23
CA 02602524 2007-10-09
. . .
section 2 reaches a predetexmined value, the temperature-responsive valve
12 is closed to stop the suction.
After heating the reaction vesseJ. 1, the steam is condensed and
rendered into condensate, which flows through the pipe line 21 down into
the condensate recovering unit 6, - By supplying the heating steam having a
predetermined pressure, i.e. a predetermined temperature into the jacket
section 2 from which the air'has been elianninated, the reaction unit 1 is
heated by the steam of the predetermined temperature. For instance,
when steam having a pressure below the atmospheric pressure and 60 C is
supplied via the pressure control valve 7, the reaction vessel 1 is heated at
6o4c.
When the inside of the jacket section 2 is set at such pressure below
the atmospheric pressure, the atmospheric pressure may act on the
respective connections, so that a portion of atmospheri.c air may enter the
jacket section 2 and this air or air mixed in the supplied steam may cause
accumulation of air inside the jacket section, whereby the temperature is
reduced due to heat discharge. Then, this temperature drop is detected by
the temperature-responsive cylinder 17 to open the temperature=responsive
valve 12 thereby to establish communication between the suction'chamber
13 of the ejector 5 and the jacket section 2. Then, with each resultant
development of suction force inside the suction chamber 13 of the ejector 5,
the air remaitvng in the jacket seetion 2 is sucked into the suction chamber
13 and exhausted to the outside. In this way, according to the present
embodiment, with the valve means, not only air present in the initial state
of the steam-heating apparatus but aLso air acc'umulated during the
subsequent heating process may be sucked and exhausted to the outside by
the steam ejector 5.
(fifth mode of embodiment)
24
CA 02602524 2007-10-09
I A 1
A ffth mode of embod'unent of a steam-heating apparatus will he
described with reference to Fig. 5 in which a reaction vessel I is employed as
a heat exchanger.
In the following discussion, the same construction as that of the
foregoing embodiment will be omitted.
In the steam-heating apparatus shown in Fig. 5, a jacket section 2
formed as a heating section in the outer periphery of the. reaction vessel 1
is
connected to a steam supply pipe 3. Further, the steam supply pipe 3 is
connected via a pipe line 9 to a high-pressure control fluid inlet 10 of a
condensate recovering unit 6. The condensate recovering unit 6 includes a
condensate returning outlet 24, which in turn is connected to a condensate
pressure-transporting pipe line 26 incorporating an'ejector 5, and a suction
chamber 13 of the ejector 5 and the jacket section 2 are connected with each
other via a pipe line 15.
The condensate pressure-transporting pipe line 26 incorporates a
check valve 25. This check valve 25 aIlows only unidirectional fluid
passage from the condensate recovering unit 6 to the outside.
The condensate pressure-transporting pipe line 26 is connected to
the ejector 5. The suction chamber 13 of the ejector 5 and the jacket section
2 are communicated with each other by a pipe line 15 incorporating a
shutoff valve 29 and a temperature-responsive valve 12. In this
embodiment, the shutoff valve 29 and the temperature-responsive valve 12
together constitute a valve means.
In this embodiment, like the foregoing embodiments, the
temperature-responsive valve 12 is constructed as a self-actuated
temperature control valve induding a temperature-responsive cylinder 17
mounted to a porti.on of the jacket section 2 where accumulation of air tends
to occur and an actuator portion 18 of the temperature-responsive valve 12,
the cylinder 17 and the actuator portion 18 being connected to each other
via a flexible tube 19.
CA 02602524 2007-10-09
. . .
Like the foregoing embodiments, the condensate recovering unit 6
doses the high-pressure control fluid inlet 10 and also opens the exhaust
returning outlet 27 when an unillustrated float contained in the unit 6 is
located at a lower position, whereby condensate inside the jacket section 2 is
caused to flow down into the recovering unit 6 via the pipe line 21, the check
valve 23 and the condensate inlet 20. Then, when the condensate is
gradually accumulated within the recovering unit 6 to push up the float to a
predetermined upper position, the unit closes the exhaust returning outlet
27 and opens the high-pressure control fluid inlet 10, whereby high-
pressure steam as a high-pressure control fluid is allowed into the unit 6 via
the steaYn supply pipe 3 and the condensate contained therein is pressure-
transported via the condensate returning outlet 24, the check valve 25 and
the pipe line 26 to a condensate recoveri.ng area, where the condensate is
recovered.
And, each time the high-pressure steam as a high-pressure control
fluid is supplied from the pipe line 26, the high-pressure steam is caused to
pass also the ejector 5, whereby a suction force can be developed in the
suction chamber 13.
In Fig. 5, when an object is to be heated inside the reaction vessel 1,
fixst, steazn in the steam supply pipe 3 is supplied via the pressure control
valve 7 to the jacket section 2. In the case of this embodiment, since the
pipe line 15 includes a branch pipe 112 and a shutoff valve 16, the remaining
ajr i.nitiaIly present inside the jacket section 2 may be exhausted by opening
the shutoff valve 16. That is to say, by supplying steam via the pressure
control valve 7 to the jacket section 2 and also opening the shutoff valve 16,
the air remaining inside the jacket section 2 is forced out by means of the
steam.
Further, wheri some air remains inside the jacket section 2, the
temperature inside the jacket section 2 has dropped. Hence, the
temperature-responsive valve 12 is opened so as to establish communication
26
CA 02602524 2007-10-09
.. ~
between suction chamber 13 of the steam ejector 5 and the jacket section 2.
So that, with each development of suction force inside the suction chamber
13 of the ejector 5, the remaining air inside the jacket section 2 is sucked
and exhausted to the outside. When the temperature inside the jacket
section 2 reaches a predetermined value, the temperature-responsive valve
12 is closed to stop the suction.
When the inside of the jacket section 2 is set at such pressure below
the atmospheric pressure, the atmospheric pressure may act on the
respective connections of the jacket section 2, so that a portion of
atmospheric air may enter the jacket section 2 and this air or air mixed in
the supplied steam may cause accumulation of air inside the jacket section 2,
whereby the temperature is reduced due to heat discharge. Then, this
temperature drop is detected by the temperature-responsive cylinder 17 to
open the temperature-responsive valve 12 thereby to establish
communication between the suction chamber 13 of the ejector 5 and the
jacket section 2. Then, with each resultant development of suction force
inside the suction chamber 13 of the ejector 5, the air remaining in the
jacket section 2 is sucked into the suction chamber 13 and exhausted to the
outside. In this way, according to the present embodiment, not with the
valve means, only air present in the initial state of the steam-heating
apparatus but also air accumulated during the subsequent heating process
may be sucked and exhausted to the outside by the steam ejector 5.
In the fourth and fifth modes of embodiment described above, the
valve means comprises the shutaffvalve 29 and the temperature-responsive
valve 12. Instead, the valve means may comprise only either the shutoff
valve or the temperature-responsive valve. Further, it is also possible to
employ a check valve which allows only unidirectional fluid passage from
the jacket section 2 to the suction chamber 13, not allowing fluid passage in
the reverse direction.
In the foregoing modes of embodiment, the temperature-responsive
27
CA 02602524 2007-10-09
valve 12 is provided as a self-actuated type temperature-responsive valve
including the temperature-responsive cylinder 17 and the actuator portion
18 connected to each other via the flexible tube 19. Instead, this
temperature-responsive valve may comprise a combination of a temperature
sensor or an oxygen sensor for detecting presence of air and a controller.
Industrial Applicability
As described above, the steam-heating apparatus relating to the
present invention heats an object placed in a heat exchanger by means of
steam supplied into a heating section. And, this apparatus is useful as a
steam-heating apparatus which allows heating the object with high
temperature precision without adverse effect of e.g. temperature
unevenness in the heating section by sucking and exhaust air accumulated
inside the heating seation. as needed. This apparatus is particularly useful
as a steam-heating apparatus suitable for a relatively low heating
temperature ranging around 1009C. Specifically, the apparatus is suitable
as a steam-heating apparatus for use in steam-heating of various reaction
vessels employed for polymerization reaction, etc., a distilling apparatus for
food products, a condensing apparatus, or a sterilizer.
28
