JP4583583B2 - Steam heating device - Google Patents

Description

[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for heating an object to be heated with steam, and more particularly to a steam heating apparatus suitable for heating at a relatively low temperature of about 100 ° C. Specifically, it is used for steam heating of various reaction kettles used for polymerization reactions and the like, food distillers, concentrators, and sterilizers. The object to be heated in these cases often causes thermal damage due to a slight temperature change, and it is necessary to maintain the heating temperature with high accuracy.
[0002]
[Prior art]
A conventional steam heating apparatus is disclosed in, for example, Japanese Patent Application Laid-Open No. 7-328422. This is a heating steam supply pipe connected to the heating section, a condensate recovery device that discharges the condensate generated by heating, and a replacement fluid supply pipe that replaces the air in the heating section. The steam can be heated at a low temperature of 100 ° C. or lower by eliminating the air in the heating section with a replacement fluid and reducing the pressure.
[0003]
[Problems to be solved by the invention]
In the above conventional one, since the condensate generated in the heating unit flows into the condensate recovery device by natural flow based on the inflow head, the condensate in the heating unit is reduced when the amount of condensate generated increases. There was a problem that the entire heating unit could not be uniformly heated by steam because the heating unit could not be quickly discharged without stagnation and part of the heating unit was covered with condensate.
[0004]
Therefore, the subject of this invention is obtaining the steam heating apparatus which can maintain steam heating temperature to a predetermined value accurately, without making the condensate which generate | occur | produced in the heating part stay.
[0005]
[Means for Solving the Problems]
The means of the present invention taken in order to solve the above-mentioned problem is to supply steam to the heating unit to steam-heat the object to be heated, and to pump the condensate generated by the heating to a predetermined location by a condensate pump. A gas-liquid separation container that separates condensate and steam is disposed between the heating unit and the condensate pump, and the gas-liquid separation container is formed of a cylindrical container, and the gas-liquid separation is performed at the center. A cylindrical pipe with a smaller diameter than the container is attached with a gap at the lower end, a condensate discharge pipe having a smaller diameter than that of the cylindrical pipe is attached to the lower part of the cylindrical pipe, and the condensate flow of the condensate pump is connected to the condensate discharge pipe by the pipe. A heat exchange means for condensing the vapor in the gas-liquid separation container is attached while being connected to the inlet, and the heat exchange means is formed by a cooling pipe spirally surrounding the outer circumference of the cylindrical pipe .
[0006]
DETAILED DESCRIPTION OF THE INVENTION
Condensate generated in the heating section reaches the gas-liquid separation container and part of it is re-evaporated to become steam. By installing the heat exchange means in the gas-liquid separation container, the re-evaporated steam is cooled and condensed by the heat exchange means, so that its volume rapidly decreases, and the gas-liquid separation container has a negative pressure below atmospheric pressure. It becomes a state. When the inside of the gas-liquid separation container is in a negative pressure state, the condensate generated in the heating unit quickly flows down to the gas-liquid separation container due to the pressure difference and does not stay in the heating unit.
[0008]
【Example】
In a present Example, the example of the jacket part 2 of the reaction kettle 1 is shown as a heating part. In FIG. 1, a gas-liquid separation container 3 connected to a jacket portion 2 and a condensate pump 4 connected to the lower part of the gas-liquid separation container 3 constitute a steam heating device.
[0009]
A steam supply pipe 5 for supplying steam for heating to the jacket portion 2 is connected via a valve 6. Steam with a predetermined pressure or temperature is supplied from the valve 6 to the jacket part 2 to heat the object to be heated in the reaction kettle 1 (not shown).
[0010]
It connects with the upper side surface of the gas-liquid separation container 3 through the pipe line 7 from the lower part of the jacket part 2. FIG. The gas-liquid separation container 3 is formed of a cylindrical container, and a cylindrical pipe 8 having a smaller diameter than that of the gas-liquid separation container 3 is attached at the center with a gap 9 provided at the lower end. A condensate discharge pipe 10 having a smaller diameter than the cylindrical pipe 8 is attached to the lower part of the cylindrical pipe 8. The condensate discharge pipe 10 is connected to the condensate inlet 12 of the condensate pump 4 by a pipe 11.
[0011]
The condensate discharge pipe 10 is attached so that the upper end of the condensate discharge pipe 10 is positioned a predetermined length above the lower end of the cylindrical pipe 8. A liquid reservoir 13 is formed by the outer periphery of the condensate discharge pipe 10, the inner and outer periphery of the cylindrical pipe 8 and the lower inner periphery of the gas-liquid separation container 3. A valve 14 and a pipe line 15 are attached to the upper end of the cylindrical pipe 8, and the valve 14 is opened so that it can communicate with the atmosphere.
[0012]
A cooling pipe 16 as a heat exchanging means is attached above the inside of the gas-liquid separation container 3. The cooling pipe 16 is formed by spirally surrounding the outer periphery of the cylindrical pipe 8. The cooling fluid is supplied from the cooling fluid supply pipe 17 and condensed by cooling the vapor in the gas-liquid separation container 3 to be condensed water. Then, it is discharged out of the system from the cooling fluid take-out pipe 18 or is sent to a separate hot water use location.
[0013]
The steam supply pipe 5 is branched and connected to the upper part of the gas-liquid separation container 3 via a pipe line 19 and a valve 20. The branch line 19 ensures a reduced pressure state in the gas-liquid separation container 3 by supplying a desired amount of steam when the amount of re-evaporated steam in the gas-liquid separation container 3 is small or fluctuates. Is for.
[0014]
A valve 21 and a check valve 22 are attached to the pipe 11 connecting the condensate discharge pipe 10 and the condensate inlet 12 of the condensate pump 4. The check valve 22 allows passage of fluid from the condensate discharge pipe 10 only in the direction of the condensate pressure pump 4, and does not allow passage of fluid in the reverse direction. The valve 21 is for adjusting the amount of condensate flowing down to the condensate pressure-feed pump 4.
[0015]
A condensate pressure feed line 26 is also connected to the condensate pressure feed port 23 of the condensate pressure feed pump 4 via a check valve 24 and a valve 25. The check valve 24 allows fluid to pass only in the outward direction from the condensate pump 4 to the condensate pump line 26 side.
[0016]
A high-pressure steam inlet 28 connected to a steam pipe 27 branched from the steam supply pipe 5 is provided above the condensate pressure pump 4. A high-pressure steam outlet 29 is provided on the side of the high-pressure steam inlet 28.
[0017]
The condensate pump 4 has a high-pressure steam inlet 28 closed and a discharge outlet 29 open when a float (not shown) disposed therein is located in the lower part, and is opposite to the pipe 11 and the valve 21. Condensate in the gas-liquid separation container 3 flows into the condensate pressure feed pump 4 through the stop valve 22 and the condensate inlet 12.
[0018]
When condensate accumulates in the condensate pump 4 and a float (not shown) is positioned at a predetermined upper portion, the discharge port 29 is closed, while the high-pressure steam inlet 28 is opened, and the high-pressure steam is discharged from the steam pipe 27. Flows into the condensate pressure pump 4, and condensate accumulated in the condensate is pumped to a predetermined condensate pressure destination via a pressure feed port 23, a check valve 24, a valve 25, and a condensate pressure feed line 26. .
[0019]
When the condensate is pumped and the liquid level in the condensate pump 4 is lowered, the inlet 28 is closed again and the outlet 29 is opened, so that the condensate is fed into the pump 4 from the condensate inlet 12. It flows down to. By repeating such an operation cycle, the condensate pressure feed pump 4 pumps the condensate in the gas-liquid separation container 3.
[0020]
In the initial stage of heating of the reaction vessel 1, non-condensable air stays in the jacket portion 2, and no liquid exists in the liquid reservoir portion 13 below the gas-liquid separation container 3. When the valve 6 is opened in this state and the steam for heating is supplied to the jacket part 2, the air in the jacket part 2 is pushed out by the steam and reaches the gas-liquid separation container 3, and the lower liquid reservoir part where no liquid exists. 13, the gap 9, the inside of the cylindrical pipe 8, the valve 14, and the conduit 15 to be discharged outside.
[0021]
As the air is discharged, condensate generated by initial heating of the reaction kettle 1 flows into the gas-liquid separation container 3 and accumulates in the liquid reservoir 13, and part of it is re-evaporated and re-evaporated. It becomes steam and accumulates above the gas-liquid separation container 3. By supplying the cooling fluid to the cooling pipe 16, the re-evaporated steam is condensed again to become condensate, and its volume is rapidly reduced, so that the gas-liquid separation container 3 is in a reduced pressure state below atmospheric pressure. Due to the reduced pressure state, the condensate generated by heating in the jacket portion 2 is sucked into the gas-liquid separation container 3 and collected in the liquid reservoir 13.
Condensate accumulated in the liquid reservoir 13 flows down into the pump 4 when the outlet 29 of the condensate pressure pump 4 is opened, and when a predetermined amount is accumulated in the pump 4, a float (not shown) rises and the outlet 29 Is closed, and at the same time, the high-pressure steam inlet 28 is opened, and is pumped from the condensate pressure feed port 23 to a predetermined location with the pressure of the high-pressure steam.
[0023]
【The invention's effect】
As described above, according to the present invention, the gas-liquid separation container for separating the condensate and the steam is disposed between the heating unit and the condensate pressure feeding device, and the heat exchange means for condensing the steam in the gas-liquid separation container is attached. As a result, the condensate generated in the heating unit is not retained, the entire heating unit can be uniformly heated with steam, and the steam heating temperature can be accurately maintained at a predetermined value.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of a steam heating apparatus according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Reaction kettle 2 Jacket part 3 Gas-liquid separation container 4 Condensate pressure feed pump 5 Steam supply pipe 8 Cylindrical pipe 10 Condensate discharge pipe 12 Condensate inlet 16 Cooling pipe 23 Condensate pressure feed inlet 28 High pressure steam inlet 29 Vent

Claims (1)

Steam is supplied to the heating section to steam-heat the object to be heated, and the condensate generated by heating is pumped to a predetermined location by a condensate pump. In the condensate pump between the heating section and the condensate pump And a gas-liquid separation container for separating the vapor, the gas-liquid separation container is formed by a cylindrical container, and a cylindrical pipe having a smaller diameter than the gas-liquid separation container is attached to the center portion with a gap at the lower end, A condensate discharge pipe having a smaller diameter than that of the cylindrical pipe is attached to the lower part of the cylindrical pipe, and the condensate discharge pipe is connected to the condensate inlet of the condensate pump by the pipe and the vapor in the gas-liquid separation container is condensed. A steam heating apparatus , wherein a heat exchange means is attached , and the heat exchange means is formed of a cooling pipe that spirally surrounds the outer periphery of the cylindrical pipe .

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