CN210892169U - Novel conduction oil furnace system - Google Patents
Novel conduction oil furnace system Download PDFInfo
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- CN210892169U CN210892169U CN201922008640.8U CN201922008640U CN210892169U CN 210892169 U CN210892169 U CN 210892169U CN 201922008640 U CN201922008640 U CN 201922008640U CN 210892169 U CN210892169 U CN 210892169U
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- conduction oil
- oil
- oil furnace
- heat conduction
- separator
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- 239000003921 oil Substances 0.000 claims abstract description 165
- 239000010724 circulating oil Substances 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims description 12
- 239000002699 waste material Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model provides a novel heat conduction oil furnace system, which relates to the technical field of heating furnaces and comprises a heat conduction oil furnace, a user side, a degasser, a circulating oil pump and a separator, wherein the heat conduction oil furnace, the user side, the degasser and the circulating oil pump are sequentially connected end to end and communicated to form a circulating system; the separator is arranged above the heat-conducting oil furnace, is simultaneously connected and communicated with the heat-conducting oil furnace and the deaerator, and is used for separating low-temperature volatile heat-conducting oil components discharged from the heat-conducting oil furnace. The utility model overcomes traditional heat conduction system only can be with moisture content from the manual discharge in the low-order oil tank, but can't separate low temperature volatile heat conduction oil component from qualified heat conduction oil.
Description
Technical Field
The utility model belongs to the technical field of the heating furnace technique and specifically relates to a novel conduction oil furnace system is related to.
Background
In the operation process of the heat conduction oil furnace, because part of low-temperature volatile components exist in the heat conduction oil, in order to ensure that moisture in the heat conduction oil is removed in the temperature rise process of the heat conduction oil furnace, a deaerator, a high-level oil tank, a low-level oil tank and the like need to be arranged in a heat conduction oil pipeline system. However, the existing heat-conducting oil pipeline system can manually discharge water from the low-level oil tank, but cannot separate the low-temperature volatile heat-conducting oil component from the qualified heat-conducting oil.
Therefore, how to ensure that the low-temperature volatile heat conduction oil component is continuously and automatically separated from the circulating system is a technical problem to be solved urgently by the technical personnel in the field.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a novel conduction oil furnace system to there is the low temperature to volatilize the conduction oil component among the solution prior art and can not follow continuous, autosegregation's technical problem in the circulation system.
In order to achieve the above purpose, the utility model provides a following technical scheme:
the utility model provides a pair of novel conduction oil furnace system, including conduction oil furnace, user side, degasser, circulating oil pump and separator, wherein:
the heat-conducting oil furnace, the user side, the deaerator and the circulating oil pump are sequentially connected end to end and communicated to form a circulating system;
the separator is arranged above the heat conduction oil furnace, is simultaneously connected and communicated with the heat conduction oil furnace and the deaerator, and is used for separating low-temperature volatile heat conduction oil components discharged from the heat conduction oil furnace.
Preferably, the separator is provided with an air inlet, an air outlet and a liquid outlet, the air inlet is located on one side of the separator, the air inlet is connected and communicated with the heat-conducting oil furnace, the air outlet is located above the separator, the liquid outlet is located below the separator, and the liquid outlet is connected and communicated with the deaerator.
Preferably, the liquid outlet is conical.
Preferably, the air outlet is connected and communicated with the condenser.
Preferably, the condenser also comprises a waste oil tank, wherein the waste oil tank is arranged below the condenser, and the waste oil tank is connected and communicated with the condenser.
Preferably, the system further comprises an expansion tank which is connected with and communicated with the deaerator;
the separator is mounted slightly above the expansion tank.
Preferably, the expansion tank is connected with the expansion tank and communicated with the expansion tank.
Preferably, a pipeline connecting the expansion tank and the oil storage tank extends into the bottom of the oil storage tank.
Preferably, the device further comprises a buffer tank, and the buffer tank is connected with and communicated with the deaerator.
Preferably, the buffer tank is connected and communicated with the oil storage tank.
The utility model provides a novel conduction oil furnace system has following technological effect:
the traditional heat conduction oil furnace system is formed by sequentially connecting a heat conduction oil furnace, a user side, a deaerator and a circulating oil pump end to end, and the circulating system supplies heat to the user side through heat conduction oil. However, the traditional heat transfer oil furnace system can only manually discharge moisture from the low-level oil tank, but cannot separate the low-temperature volatile heat transfer oil component from the qualified heat transfer oil. And the utility model discloses increased the separator on traditional circulation system, separator and heat conduction oil furnace intercommunication, the conduction oil that contains partial low temperature heat conduction oil component that volatilizees has realized that low temperature volatilizees the heat conduction oil component and has lasted, separates automatically from the conduction oil in the conduction oil, has overcome traditional heat conduction system's unable the defect of separating low temperature heat conduction oil component from qualified heat conduction oil.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic flow chart of a novel heat transfer oil furnace system according to an embodiment of the present invention;
fig. 2 is a side view of a separator of the novel conduction oil furnace system of fig. 1;
FIG. 3 is a top view of the separator of FIG. 2;
FIG. 4 is a side view of a condenser of the novel conduction oil furnace system of FIG. 1;
fig. 5 is a top view of the condenser of fig. 5.
Wherein, fig. 1-5:
101. a heat-conducting oil furnace; 102. a user side; 103. a deaerator; 104. a circulating oil pump; 105. a separator; 1051. an air inlet; 1052. an air outlet; 1053. a liquid outlet; 106. a condenser; 107. a waste oil tank; 108. an expansion tank; 109. a buffer tank; 110. an oil storage tank.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, the technical solutions of the present invention will be described in detail below. It is to be understood that the embodiments described are only some embodiments of the invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
In the description of the present invention, it is to be understood that the terms "center", "length", "width", "height", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "side", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in fig. 1, and are only for convenience of description and to simplify the description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore should not be construed as limiting the present invention. In the description of the present invention, "a plurality" means two or more unless otherwise specified.
Fig. 1 is a schematic flow diagram of a novel conduction oil furnace system according to an embodiment of the present invention, fig. 2 is a side view of a separator of the novel conduction oil furnace system of fig. 1, fig. 3 is a top view of the separator of fig. 2, fig. 4 is a side view of a condenser of the novel conduction oil furnace system of fig. 1, and fig. 5 is a top view of the condenser of fig. 5.
The heat conduction oil heats in the heat conduction oil furnace, owing to receive high temperature, the pyrolysis of heat conduction oil produces little molecule steam, promptly the utility model discloses the heat conduction oil component that volatilizees of low temperature.
The utility model provides a novel conduction oil furnace system, as shown in fig. 1-5, including heat conduction oil furnace 101, user 102, degasser 103, circulating oil pump 104 and separator 105.
A heat conduction oil furnace 101 and a heating device of heat conduction oil.
The user terminal 102 can use heat of the heat transfer oil.
And the degasser 103 is used for removing low-temperature volatile heat conduction oil components in the heat conduction oil.
And the circulating oil pump 104 is used for providing power for the flow of the heat conduction oil.
And a separator 105 for separating the low-temperature volatile heat transfer oil component in the heat transfer oil from the heat transfer oil.
The specific installation mode of the heat-conducting oil furnace 101, the user terminal 102, the deaerator 103, the circulating oil pump 104 and the separator 105 is as follows: the heat conduction oil furnace 101, the user end 102, the deaerator 103 and the circulating oil pump 104 are sequentially connected end to end and communicated, namely, the heat conduction oil furnace 101 is communicated with the user end 102, the user end 102 is communicated with the deaerator 103, the deaerator 103 is communicated with the circulating oil pump 104, the circulating oil pump 104 is communicated with the heat conduction oil furnace 101 to form a circulating system, heat conduction oil is heated by the heat conduction oil furnace 101 and flows through the user end 102, the user end 102 absorbs heat of the heat conduction oil, the heat conduction oil is cooled, meanwhile, the heat conduction oil carries low-temperature volatile heat conduction oil components, then, the heat conduction oil passes through the deaerator 103, and the deaerator.
The separator 105 is installed above the heat conduction oil furnace 101, the separator 105 is simultaneously connected and communicated with the heat conduction oil furnace 101 and the deaerator 103, namely after heat conduction oil discharged from the heat conduction oil furnace 101 flows through the separator 105, the separator 105 separates the heat conduction oil which is discharged from the heat conduction oil furnace 101 and carries low-temperature volatile heat conduction oil components, the separated heat conduction oil returns to the deaerator 103, and the separated heat conduction oil enters the circulation system, namely, enters the main heat conduction oil pipeline.
Specifically, the separator 105 is provided with an air inlet 1051, an air outlet 1052 and an air outlet 1053, as shown in fig. 2 and fig. 3, the air inlet 1051 is located at one side of the separator 105, the air inlet 1051 is connected and communicated with the heat-conducting oil furnace 101, the air outlet 1052 is located above the separator 105, the air outlet 1053 is located below the separator 105, the air outlet 1053 is connected and communicated with the deaerator 103, the air outlet 1053 is in a cone shape, the separated heat-conducting oil comes out from the cone-shaped air outlet 1053 and enters into the heat-conducting oil main pipeline, and the low-temperature volatile heat-conducting oil component is discharged from the air outlet 1052.
Traditional heat conduction oil furnace 101 system is only by heat conduction oil furnace 101, user end 102, degasser 103 and circulating oil pump 104 end to end connection in order, forms the circulation system, and this circulation system passes through the conduction oil and supplies heat for user end 102, only can be with moisture content manual discharge from the low-order oil tank, but can't separate low temperature volatilization heat conduction oil component from qualified heat conduction oil, and the utility model discloses separator 105 has been increased on traditional circulation system, separator 105 and heat conduction oil furnace 101 intercommunication, the conduction oil that contains partial low temperature volatilization heat conduction oil component passes through separator 105, has realized the separation of low temperature volatilization heat conduction oil component from the conduction oil, has overcome traditional heat conduction system's unable defect of separating low temperature volatilization heat conduction oil component from qualified heat conduction oil.
In a further scheme, the condenser 106 and the waste oil tank 107 are further included, as shown in fig. 1, 4 and 5, the air outlet 1052 of the separator 105 is connected and communicated with the condenser 106, the waste oil tank 107 is installed below the condenser 106, and the waste oil tank 107 is connected and communicated with the condenser 106.
The mixed gas discharged from the gas outlet 1052 of the separator 105 is connected to the condenser 106 through a pipeline, the low-temperature volatile heat conduction oil component is condensed, the low-temperature volatile heat conduction oil component carries moisture, the density of the low-temperature volatile heat conduction oil component of the liquid is smaller than that of the moisture, the low-temperature volatile heat conduction oil component is located on the upper portion of the condenser 106, and the operator periodically discharges the liquids made of two materials into different containers respectively and reasonably disposes the liquids.
In a further scheme, a certain amount of heat conduction oil needs to be stored in the heat conduction oil main pipeline in advance, when the heat conduction oil furnace 101 heats the heat conduction oil, the heat conduction oil is heated to expand, and the expansion tank 108 needs to be connected, as shown in fig. 1, the expansion tank 108 is connected and communicated with the deaerator 103, namely, the heat conduction oil in the heat conduction oil main pipeline flows into the expansion tank 108 after expanding.
Specifically, the separator 105 is installed slightly above the expansion tank 108.
In order to recover the heat transfer oil, an oil storage tank 110 is further included, as shown in fig. 1, the oil storage tank 110 is connected and communicated with the expansion tank 108, and a pipeline connecting the expansion tank 108 and the oil storage tank 110 extends into the bottom of the oil storage tank 110.
In a further scheme, the heat-conducting oil furnace further comprises a buffer tank 109, as shown in fig. 1, the buffer tank 109 is connected and communicated with the deaerator 103, the buffer tank 109 is connected and communicated with the oil storage tank 110, the heat-conducting oil furnace 101 is suddenly heated, and the buffer tank 109 plays a buffer role.
The above description is only for the specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art can easily think of the changes or substitutions within the technical scope of the present invention, and all should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (10)
1. The utility model provides a novel conduction oil furnace system which characterized in that, includes conduction oil furnace (101), user side (102), degasser (103), circulating oil pump (104) and separator (105), wherein:
the heat-conducting oil furnace (101), the user end (102), the deaerator (103) and the circulating oil pump (104) are sequentially connected end to end and communicated to form a circulating system;
the separator (105) is arranged above the heat-conducting oil furnace (101), the separator (105) is simultaneously connected and communicated with the heat-conducting oil furnace (101) and the deaerator (103), and the separator (105) is used for separating low-temperature volatile heat-conducting oil components discharged from the heat-conducting oil furnace (101).
2. The novel conduction oil furnace system as claimed in claim 1, wherein the separator (105) is provided with an air inlet (1051), an air outlet (1052) and an liquid outlet (1053), the air inlet (1051) is positioned at one side of the separator (105), the air inlet (1051) is connected and communicated with the heat conduction oil furnace (101), the air outlet (1052) is positioned above the separator (105), the liquid outlet (1053) is positioned below the separator (105), and the liquid outlet (1053) is connected and communicated with the deaerator (103).
3. The novel conduction oil furnace system as claimed in claim 2, wherein the liquid outlet (1053) is tapered.
4. The novel conduction oil furnace system as claimed in claim 2, further comprising a condenser (106), wherein the air outlet (1052) is connected and communicated with the condenser (106).
5. The novel conduction oil furnace system according to claim 4, further comprising a waste oil tank (107), wherein the waste oil tank (107) is installed below the condenser (106), and the waste oil tank (107) is connected and communicated with the condenser (106).
6. The novel conduction oil furnace system according to any one of claims 1 to 5, characterized by further comprising an expansion tank (108), wherein the expansion tank (108) is connected and communicated with the deaerator (103);
the separator (105) is mounted slightly above the expansion tank (108).
7. The novel conduction oil furnace system according to claim 6, further comprising an oil storage tank (110), wherein the oil storage tank (110) is connected and communicated with the expansion tank (108).
8. The novel conduction oil furnace system according to claim 7, wherein a pipeline connecting the expansion tank (108) and the oil storage tank (110) extends into the bottom of the oil storage tank (110).
9. The novel conduction oil furnace system according to claim 7, further comprising a buffer tank (109), wherein the buffer tank (109) is connected and communicated with the deaerator (103).
10. The novel conduction oil furnace system according to claim 9, wherein the buffer tank (109) is connected and communicated with the oil storage tank (110).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922008640.8U CN210892169U (en) | 2019-11-20 | 2019-11-20 | Novel conduction oil furnace system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922008640.8U CN210892169U (en) | 2019-11-20 | 2019-11-20 | Novel conduction oil furnace system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210892169U true CN210892169U (en) | 2020-06-30 |
Family
ID=71318903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922008640.8U Expired - Fee Related CN210892169U (en) | 2019-11-20 | 2019-11-20 | Novel conduction oil furnace system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210892169U (en) |
-
2019
- 2019-11-20 CN CN201922008640.8U patent/CN210892169U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200630 |