CN213955287U - Electric heating steam superheating system - Google Patents
Electric heating steam superheating system Download PDFInfo
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- CN213955287U CN213955287U CN202022992088.3U CN202022992088U CN213955287U CN 213955287 U CN213955287 U CN 213955287U CN 202022992088 U CN202022992088 U CN 202022992088U CN 213955287 U CN213955287 U CN 213955287U
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- 238000005485 electric heating Methods 0.000 title claims abstract description 73
- 238000009834 vaporization Methods 0.000 claims abstract description 8
- 230000008016 vaporization Effects 0.000 claims abstract description 8
- 239000003921 oil Substances 0.000 claims description 160
- 239000007788 liquid Substances 0.000 claims description 31
- 239000010724 circulating oil Substances 0.000 claims description 11
- 238000013021 overheating Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 58
- 238000010438 heat treatment Methods 0.000 abstract description 37
- 229920006395 saturated elastomer Polymers 0.000 abstract description 17
- 238000007670 refining Methods 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 229910000831 Steel Inorganic materials 0.000 abstract description 6
- 239000010959 steel Substances 0.000 abstract description 6
- 239000002918 waste heat Substances 0.000 abstract description 4
- 238000005338 heat storage Methods 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- 239000000446 fuel Substances 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000005674 electromagnetic induction Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 241001062472 Stokellia anisodon Species 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- -1 calcium carbonate Chemical class 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model discloses an electrical heating steam superheating system, include conduction oil electric heater unit (10) through the pipe connection, oil vapour heat transfer device (20), oil and gas separator (30) and expansion tank (40), conduction oil electric heater unit (10) can heat the conduction oil, conduction oil in the conduction oil electric heater unit (10) can get into in oil vapour heat transfer device (20), oil vapour heat transfer device (20) outer joint steam input pipeline (21) and steam output line (22), the steam in oil vapour heat transfer device (20) can be heated to the conduction oil in oil vapour heat transfer device (20). The electric heating steam superheating system takes electric energy as a heat source, adopts heat conduction oil as an intermediate heat exchange medium, heats converter vaporization waste heat saturated steam into micro superheated steam for a steam pump of an RH vacuum refining furnace of a steel plant, and meets the requirement of an intermittent production steam system of the refining furnace.
Description
Technical Field
The utility model relates to an electrical heating steam superheating system.
Background
Steel enterprises often adopt a refining mode of vacuumizing by a steam jet pump to smelt clean steel, the steam jet pump needs superheated steam as a power source, and the production characteristic is a periodic intermittent operation mode.
Currently, the main sources of superheated steam used by steam jet pumps are: first, a rapid boiler using fuel combustion as a heat source generates superheated steam. And secondly, producing superheated steam by adopting medium-temperature medium-pressure steam and steam with parameters above in the power plant through temperature reduction and pressure reduction. Thirdly, saturated steam is produced by utilizing the production process of a steel converter and an electric furnace, and superheated steam is prepared by heating. Various technologies and products are available for carrying out superheating treatment on converter and electric furnace self-produced saturated steam, such as: gas-fired steam superheating, micro-superheating heat storage systems, electric superheating, electromagnetic superheating, molten salt heat storage superheating, heat conduction oil heat storage superheating and the like.
The rapid boiler and gas-fired steam superheating using the traditional fuel combustion as a heat source has the defects of high environmental protection limitation on pollutant emission, complex heat source system, high initial investment, huge equipment, long starting time, serious heat energy waste during the intermission, relatively low heat efficiency and the like.
The temperature reduction, pressure reduction and overheating which take medium-temperature medium-pressure steam and above parameter steam in a power plant as a heat source are influenced by production factors of an upstream power plant, high-quality heat energy is degraded and utilized, and the system energy efficiency is low. Meanwhile, the intermittent production system of the refining furnace puts high requirements on the operation and the load control of a power plant.
The electric energy is used as a heat source to directly heat the saturated steam, an intermittent production system of the refining furnace and the characteristics of an electric heating body are not considered, the electric heating body and the saturated steam exchange heat no matter a resistance heating mode or an electromagnetic heating mode is adopted, and the accurate control of the temperature of the superheated steam is difficult to realize by a mode of directly heating the saturated steam by the electric heating body for the intermittent steam-using degree of the refining furnace. When the refining furnace uses steam, the electric heating body is scoured and cooled by the steam with a certain speed. When the refining furnace is stopped instantly, the electric heating body can not be cooled under the condition of no steam circulation and is in a dry-burning state, and the electric heating body is easy to burn when running for a long time in a resistance heating mode. Saturated steam carries liquid water more or less, and liquid water has certain hardness, and liquid water evaporates on the electric heating body surface, and hardness etc. remain on the electric heating body surface, and long-term use electric heating body surface scale deposit is serious, influences heat transfer efficiency. The service life of the electric heating body in the resistance heating mode is short, the replacement rate is high, the power consumption rate in the electromagnetic induction mode is increased, and the service life of the electric heating body is shortened.
The micro-superheat variable-pressure heat accumulator system taking the micro-superheat variable-pressure heat accumulator system as a heat source does not consider the fluctuation of the high-pressure steam pressure and the temperature of the heat accumulator and the working condition of the heat release tail end of the heat accumulator, and cannot accurately control the superheat degree of outlet steam or even meet the requirements of designated users.
The molten salt is used as an intermediate medium to indirectly heat saturated steam, an immersed heat exchanger is adopted, the heat exchange strength is low, and the accurate adjustment of the temperature of the superheated steam is difficult to realize. In addition, the molten salt has complex components, and the molten salt may contain some impurity salts, such as calcium carbonate, which may form heat scale on the surface of the heated pipe, thereby complicating the system or affecting the continuous service life of the system.
The mode of indirectly heating saturated steam by taking heat conduction oil as an intermediate medium and the mode of arranging the electric heater in the hot oil tank with a large volume are adopted, the flow velocity of the heat conduction oil in the hot oil tank cannot guarantee the flow velocity allowed by heat exchange of the heat conduction oil, and the surface heat exchange strength of the electric heater is low, so that the oil film on the surface of the electric heater is easy to crack due to the overtemperature. Meanwhile, the hot oil tank runs at normal pressure, and high-temperature heat conduction oil is easy to oxidize and deteriorate.
SUMMERY OF THE UTILITY MODEL
In order to change converter vaporization waste heat saturated steam into little superheated steam and supply steelmaking technology steam pump to use, the utility model provides an electrical heating steam superheating system uses the electric energy as the heat source, adopts the conduction oil as middle heat transfer medium, supplies the steel mill RH vacuum refining furnace steam pump to use for little superheated steam with converter vaporization waste heat saturated steam heating, satisfies the steam system for refining furnace intermittent type formula production.
The utility model provides a technical scheme that its technical problem adopted is: the utility model provides an electrical heating steam superheating system, including the conduction oil electric heater unit through the pipe connection, oil vapour heat transfer device, oil and gas separator and expansion tank, conduction oil electric heater unit can heat the conduction oil, the conduction oil in the conduction oil electric heater unit can get into in the oil vapour heat transfer device, the conduction oil in the conduction oil electric heater unit can also get into in the expansion tank, the conduction oil in the oil vapour heat transfer device can get into in the oil gas separator, the conduction oil in the oil gas separator can get into in the conduction oil electric heater unit, the gas in the oil gas separator can get into in the expansion tank, the conduction oil in the expansion tank can get into in the conduction oil electric heater unit, oil vapour heat transfer device connects steam input pipeline and steam output pipeline outward, the conduction oil in the oil vapour heat transfer device can heat the steam in the oil vapour heat transfer device.
The heat conduction oil electric heating device comprises a plurality of electric heating units which are arranged in parallel and controlled in a grouping mode.
The outlet of the heat conduction oil electric heating device is connected with the heat conduction oil inlet of the oil-gas heat exchange device through a first oil pipeline, and the heat conduction oil outlet of the oil-gas heat exchange device is connected with the inlet of the oil-gas separator through a second oil pipeline.
The liquid outlet of the oil-gas separator is connected with the inlet of the heat-conducting oil electric heating device through a third oil pipeline, and a circulating oil pump is arranged on the third oil pipeline.
The expansion tank comprises a liquid inlet, a gas inlet, a liquid outlet and an exhaust port, the liquid inlet, the gas inlet and the exhaust port are all positioned at the upper part of the expansion tank, and the liquid outlet is positioned at the lower part of the expansion tank.
And a liquid outlet of the expansion tank is connected with a third oil pipeline through a fourth oil pipeline, and the joint of the fourth oil pipeline and the third oil pipeline is positioned between a liquid outlet of the oil-gas separator and the circulating oil pump.
The gas outlet of the oil-gas separator is connected with the gas inlet of the expansion tank through a gas exhaust pipeline, the first oil pipeline is provided with a safety valve, and the discharge port of the safety valve is connected with the liquid inlet of the expansion tank through a fifth oil pipeline.
The expansion tank is positioned above the heat-conducting oil electric heating device, the oil-gas heat exchange device and the oil-gas separator.
One end of a steam input pipeline is connected with a steam inlet of the oil-steam heat exchange device, the other end of the steam input pipeline is connected with a main steam pipe of a steam heat accumulator of the converter vaporization system, one end of a steam output pipeline is connected with a steam outlet of the oil-steam heat exchange device, and the other end of the steam output pipeline is connected with a steam cylinder of the steam jet pump.
The utility model has the advantages that:
1. the electric energy is used as a steam heating heat source, so that the emission of fuel combustion pollutants to the environment is avoided.
2. The heat conduction oil is used as the intermediate heat medium, and the electric energy can be converted into high-energy electric energy by utilizing the heat storage property and high liquid phase operation temperature of the heat conduction oil
The saturated steam heating medium has good storability and fluidity, and can provide stability for steam with large volatilityBut a sufficient intermediate heat source.
3. The heat conducting oil is used as the intermediate heat medium, and the characteristic that the solubility of salt in the heat conducting oil is low is utilized to ensure the service life of the electric heating body.
4. Through setting up the circulating oil pump, the conduction oil is with the mode transmission heat that follows forced circulation, and the intensive heat transfer makes the conduction oil that flows into conduction oil electric heater unit have certain velocity of flow simultaneously.
5. By adopting a combination mode of a plurality of heating units, grouping and compiling the heating units and adopting a multi-stage heating mode, the instant acquisition of higher heat load is ensured, and the problem of small power of a single heating body in the prior art is avoided. Meanwhile, the heat conducting oil is quickly heated, and the purpose of high-efficiency heating is achieved.
6. By adopting the multi-unit low-power heating body, the phenomenon that the oil film is cracked at an excessive temperature due to overlarge surface heat flow density when a heating body with larger power is adopted is avoided.
7. By adopting the multi-unit low-power heating body grouping electricity and a multi-stage heating mode, the heat load can be well adjusted.
8. By adopting the multi-unit low-power heating body, the impact of frequent start and stop of the high-power electric heating body on the power grid is avoided, and the service life of the electric heating body is prolonged.
9. The heat conduction oil is subjected to heat exchange with the electric heating body within a safe flow rate range by independently configuring the heat conduction oil electric heating device and utilizing the circulating oil pump to pressurize and forcibly circulate, so that the overtemperature and cracking of the heat conduction oil film on the surface of the electric heating body are avoided.
Drawings
The accompanying drawings, which form a part of the present application, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the invention and not to limit the invention.
Fig. 1 is a schematic view of an electrically heated steam superheating system according to the present invention.
Fig. 2 is a schematic view of a conduction oil electric heating device.
Fig. 3 is a schematic view of an oil-gas heat exchanger device.
Fig. 4 is a schematic diagram of an oil separator.
Fig. 5 is a schematic view of an expansion tank.
10. A heat conducting oil electric heating device; 20. an oil-gas heat exchange device; 30. an oil-gas separator; 40. an expansion tank;
11. an electrical heating unit; 12. a power source;
21. a steam input line; 22. a steam output line; 23. a heat transfer oil inlet; 24. a heat conducting oil outlet; 25. a steam inlet; 26. a steam outlet;
41. a liquid inlet; 42. an air inlet; 43. a liquid outlet; 44. an exhaust port; 45. an exhaust pipe;
51. a first oil delivery line; 52. a second oil delivery line; 53. a third oil delivery line; 54. a fourth oil delivery line; 55. a fifth oil delivery line; 56. a circulating oil pump; 57. an exhaust line; 58. a safety valve.
Detailed Description
It should be noted that the embodiments and features of the embodiments in the present application may be combined with each other without conflict. The present invention will be described in detail below with reference to the accompanying drawings in conjunction with embodiments.
An electric heating steam superheating system comprises a heat-conducting oil electric heating device 10, an oil-gas heat exchange device 20, an oil-gas separator 30 and an expansion tank 40 which are connected through pipelines, wherein the heat-conducting oil electric heating device 10 can heat conducting oil, the heat conducting oil in the heat-conducting oil electric heating device 10 can enter the oil-gas heat exchange device 20, the heat conducting oil in the heat-conducting oil electric heating device 10 can also enter the expansion tank 40, the heat conducting oil in the oil-gas heat exchange device 20 can enter the oil-gas separator 30, the heat conducting oil in the oil-gas separator 30 can enter the heat-conducting oil electric heating device 10, the gas in the oil-gas separator 30 can enter the expansion tank 40, the heat conducting oil in the expansion tank 40 can enter the heat-conducting oil electric heating device 10, the oil-gas heat exchange device 20 is externally connected with a steam input pipeline 21 and a steam output pipeline 22, the heat conducting oil in the oil-gas heat exchange device 20 can heat steam in the oil-gas heat exchange device 20, as shown in fig. 1-5.
The utility model discloses an electric energy replaces conventional fuel burning heat source as the heat source, has solved the burning pollutant emission problem. The heat conduction oil is used as the intermediate heat medium, so that the electric heating body directly heats the heat conduction oil in a contact mode, and the electric heating body does not directly heat saturated steam in a contact mode, and the problem that the surface of the electric heater is easy to scale and oxidize is solved. The heat conduction oil is used as an intermediate heat medium, and the problem of unstable temperature of superheated steam output by the oil-gas heat exchange device is solved by utilizing the heat storage characteristic of the heat conduction oil.
In this embodiment, the conduction oil electric heating device 10 may include a plurality of electric heating units 11 therein, the plurality of electric heating units 11 are connected in parallel, and the plurality of electric heating units 11 are controlled in groups to solve the problem of adjusting the heat load. The electric heating unit 11 is connected with a power supply 12, and the electric heating unit 11 can adopt a resistance or electromagnetic induction heating mode.
The plurality of electric heating units 11 can be divided into a plurality of electric adding groups, each electric adding group can contain at least one electric heating unit 11, and the working number and the working position of the electric adding group can be controlled according to requirements. The combined mode of a plurality of heating units, the grouping compilation of heating units and the multistage heating mode solve the problems of small load and slow temperature rise of a single heating unit. By adopting the multi-unit low-power electric heating unit 11, the problem of oil film over-temperature cracking caused by overlarge heat flux density on the surface of a high-power heating body can be solved. By adopting the multi-unit low-power electric heating unit 11, the impact of frequent start and stop of the heating body on a power grid can be solved, and the service life of the electric heating body is prolonged.
In this embodiment, the outlet of the conduction oil electric heating device 10 is connected with the conduction oil inlet 23 of the oil-gas heat exchanging device 20 through a first oil pipeline 51, and the conduction oil outlet 24 of the oil-gas heat exchanging device 20 is connected with the inlet of the oil-gas separator 30 through a second oil pipeline 52. The liquid outlet of the oil-gas separator 30 is connected with the inlet of the heat-conducting oil electric heating device 10 through a third oil pipeline 53, and a circulating oil pump 56 is arranged on the third oil pipeline 53. The circulating oil pump 56 is arranged to transfer heat in a forced circulation mode of the heat conduction oil, so that the problem of heat transfer efficiency is solved.
In this embodiment, the expansion tank 40 includes a liquid inlet 41, a gas inlet 42, a liquid outlet 43, and a gas outlet 44, the liquid inlet 41, the gas inlet 42, and the gas outlet 44 are located at the upper part of the expansion tank 40, and the liquid outlet 43 is located at the lower part of the expansion tank 40. The expansion tank 40 is of a tank structure, heat conduction oil is located at the middle lower part in the expansion tank 40, and a gas cavity is arranged at the upper part in the expansion tank 40. An exhaust pipe 45 is connected outside the exhaust port 44, and a valve is arranged on the exhaust pipe 45.
In the present embodiment, the liquid outlet 43 of the expansion tank 40 is connected to the third flow line 53 via a fourth flow line 54, and the connection of the fourth flow line 54 to the third flow line 53 is located between the liquid outlet of the gas-oil separator 30 and the recycle oil pump 56. The gas outlet of the oil-gas separator 30 is connected with the gas inlet 42 of the expansion tank 40 through the exhaust pipeline 57, the first oil pipeline 51 is provided with a safety valve 58, the discharge port of the safety valve 58 is connected with the liquid inlet 41 of the expansion tank 40 through the fifth oil pipeline 55, and the heat transfer oil discharged from the discharge port of the safety valve 58 can enter the expansion tank 40 through the fifth oil pipeline 55.
In this embodiment, the oil-gas separator 30, the oil-gas heat exchanger 20, and the expansion tank 40 may all adopt products of the prior art, and the expansion tank 40 is located above the heat-conducting oil electric heating device 10, the oil-gas heat exchanger 20, and the oil-gas separator 30, that is, the position of the expansion tank 40 is higher than the position of the heat-conducting oil electric heating device 10, the position of the oil-gas heat exchanger 20, and the position of the oil-gas separator 30.
In the embodiment, one end of the steam input pipeline 21 is connected with the steam inlet 25 of the oil-steam heat exchanger 20, the other end of the steam input pipeline 21 is connected with the main steam pipe of the steam heat accumulator of the converter vaporization system, one end of the steam output pipeline 22 is connected with the steam outlet 26 of the oil-steam heat exchanger 20, and the other end of the steam output pipeline 22 is connected with the cylinder of the steam jet pump.
Electric heating steam superheating system uses the electric energy as the heat source, adopts the conduction oil as middle heat transfer medium, supplies the steel mill RH vacuum refining furnace steam pump to use for little superheated steam with converter vaporization waste heat saturated steam heating, satisfies the steam system for refining furnace intermittent type formula production. The utility model discloses dispose heat conduction oil electric heater unit alone, utilize forced circulation mode heating conduction oil, make the conduction oil in safe velocity of flow within range and electric heating body heat transfer, solve heating member surface heat conduction oil film overtemperature, schizolysis problem.
The operation of the electrically heated steam superheating system is described below.
High-pressure saturated steam supplied by a converter vaporization system heat accumulator enters an oil-steam heat exchanger 20 through a steam input pipeline 21 after being stabilized by a pressure regulating valve, and is heated, and the saturated steam is converted into qualified low-pressure micro-superheated steam and is supplied to a vacuum refining steam pump through a steam output pipeline 22.
High-temperature heat conduction oil supplied by the heat conduction oil electric heating device 10 is sent to the oil-gas heat exchange device 20, the high-temperature heat conduction oil exchanges heat with saturated steam in the oil-gas heat exchange device 20, the heat conduction oil after heat exchange flows into the oil-gas separator 30 to be degassed, the heat conduction oil after gas removal is pressurized by the circulating oil pump 56 and sent to the heat conduction oil electric heating device 10 to be heated again, and thus a heat conduction oil cycle is formed.
The expansion tank 40 is arranged at the highest position of the electric heating steam overheating system, the expansion tank 40 is divided into an oil space and an air space which are arranged from the lower part to the upper part, oil stored in the expansion tank 40 is used as the inlet of the circulating oil pump 56 for constant pressure, and is used as heat conduction oil to thermally expand the oil storage tank, and the air space collects gas released from the oil-gas separator 30.
The first oil pipeline 51 outside the outlet of the heat conduction oil electric heating device 10 is provided with a safety valve 58, so that the heating system is prevented from being damaged due to over-high and over-pressure oil temperature inside the heat conduction oil electric heating device 10. The heat-conducting oil electric heating device 10 is composed of a plurality of heating units 11, supplies power in groups, adjusts the electric load according to the steam supply heat load, and precisely controls the temperature of output steam by finely adjusting the circulating oil pump 56 by utilizing the heat storage characteristic of heat conduction. Meanwhile, the heat conducting oil pipeline system is provided with necessary facilities such as filtering, air discharging, oil discharging, detecting instruments and the like.
The above description is only for the specific embodiments of the present invention, and the scope of the present invention can not be limited by the embodiments, so that the replacement of the equivalent components or the equivalent changes and modifications made according to the protection scope of the present invention should still belong to the scope covered by the present patent. In addition, the utility model provides an between technical feature and the technical feature, between technical feature and technical scheme, technical scheme and the technical scheme all can the independent assortment use.
Claims (9)
1. An electric heating steam overheating system is characterized by comprising a heat conduction oil electric heating device (10), an oil-steam heat exchange device (20), an oil-gas separator (30) and an expansion tank (40) which are connected through pipelines, wherein the heat conduction oil electric heating device (10) can heat conduction oil, the heat conduction oil in the heat conduction oil electric heating device (10) can enter the oil-steam heat exchange device (20), the heat conduction oil in the heat conduction oil electric heating device (10) can also enter the expansion tank (40), the heat conduction oil in the oil-steam heat exchange device (20) can enter the oil-gas separator (30), the heat conduction oil in the oil-gas separator (30) can enter the heat conduction oil electric heating device (10), the gas in the oil-gas separator (30) can enter the heat conduction oil expansion tank (40), and the expansion tank (40) can enter the heat conduction oil electric heating device (10), the steam input pipeline (21) and the steam output pipeline (22) are connected with the outside of the oil-steam heat exchange device (20), and heat conduction oil in the oil-steam heat exchange device (20) can heat steam in the oil-steam heat exchange device (20).
2. The electrically heated steam superheating system according to claim 1, wherein the diathermic oil electric heating device (10) comprises a plurality of electric heating units (11), the plurality of electric heating units (11) being arranged in parallel, the plurality of electric heating units (11) being controlled in groups.
3. The electrically heated steam superheating system according to claim 1, wherein the outlet of the heat conducting oil electric heating device (10) is connected to the heat conducting oil inlet (23) of the oil-gas heat exchanger (20) via a first oil line (51), and the heat conducting oil outlet (24) of the oil-gas heat exchanger (20) is connected to the inlet of the oil-gas separator (30) via a second oil line (52).
4. The electrically heated steam superheating system according to claim 3, wherein the liquid outlet of the oil-gas separator (30) is connected to the inlet of the thermally conductive oil electric heating device (10) via a third oil line (53), and a circulating oil pump (56) is provided on the third oil line (53).
5. An electrically heated steam superheating system according to claim 4 wherein the expansion tank (40) comprises a liquid inlet (41), a liquid inlet (42), a liquid outlet (43) and a gas outlet (44), the liquid inlet (41), the liquid inlet (42) and the gas outlet (44) being located in the upper part of the expansion tank (40), the liquid outlet (43) being located in the lower part of the expansion tank (40).
6. An electrically heated steam superheating system according to claim 5 wherein the liquid outlet (43) of the expansion tank (40) is connected to the third flow line (53) via a fourth flow line (54), the connection of the fourth flow line (54) to the third flow line (53) being located between the liquid outlet of the gas-oil separator (30) and the recycle oil pump (56).
7. An electrically heated steam superheating system according to claim 5 wherein the gas outlet of the gas-oil separator (30) is connected to the gas inlet (42) of the expansion tank (40) via a gas discharge line (57), the first oil line (51) being provided with a safety valve (58), the discharge opening of the safety valve (58) being connected to the liquid inlet (41) of the expansion tank (40) via a fifth oil line (55).
8. The electrically heated steam superheating system according to claim 1 wherein the expansion tank (40) is located above the heat conducting oil electric heating means (10), the oil-gas heat exchange means (20) and the gas-oil separator (30).
9. The electrically heated steam superheating system according to claim 1, wherein one end of the steam input line (21) is connected to the steam inlet (25) of the oil-steam heat exchanger (20), the other end of the steam input line (21) is connected to the main steam pipe of the steam accumulator of the converter vaporization system, one end of the steam output line (22) is connected to the steam outlet (26) of the oil-steam heat exchanger (20), and the other end of the steam output line (22) is connected to the cylinder of the steam jet pump.
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| CN202022992088.3U CN213955287U (en) | 2020-12-14 | 2020-12-14 | Electric heating steam superheating system |
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| CN202022992088.3U CN213955287U (en) | 2020-12-14 | 2020-12-14 | Electric heating steam superheating system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112443828A (en) * | 2020-12-14 | 2021-03-05 | 北京京诚科林环保科技有限公司 | Electric heating steam superheating system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112443828A (en) * | 2020-12-14 | 2021-03-05 | 北京京诚科林环保科技有限公司 | Electric heating steam superheating system |
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