CN218001168U - Steam temperature and pressure reduction adjusting system - Google Patents

Steam temperature and pressure reduction adjusting system Download PDF

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Publication number
CN218001168U
CN218001168U CN202222455771.2U CN202222455771U CN218001168U CN 218001168 U CN218001168 U CN 218001168U CN 202222455771 U CN202222455771 U CN 202222455771U CN 218001168 U CN218001168 U CN 218001168U
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temperature
pressure
steam
valve
water
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CN202222455771.2U
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王炳富
蒋淑妃
王本进
周杰
方新颜
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Zhejiang Construction Co Ltd of China Construction Eighth Engineering Division Co Ltd
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Zhejiang Construction Co Ltd of China Construction Eighth Engineering Division Co Ltd
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Abstract

The utility model provides a steam temperature and pressure reduction regulating system, wherein a steam inlet pipe is connected with a steam outlet pipe through a first electric gate valve, a first electric pressure reducing valve, a second electric gate valve and a temperature and pressure reducing valve in sequence, and a control device respectively regulates the first and the second electric gate valves and a first electric water feeding valve according to the pressure of high-temperature high-pressure steam, the pressure of temperature and pressure reducing steam and the expected pressure; the desuperheating water source is respectively connected with a first electric water supply valve and a second electric water supply valve through a first desuperheating water conveying device and a second desuperheating water conveying device through pipelines, then is respectively connected with a first atomizing nozzle and a second atomizing nozzle which are inserted into the desuperheating pressure reducer through pipelines, and a control device opens and closes the first desuperheating water conveying device and the second desuperheating water conveying device according to the temperature of high-temperature high-pressure steam, the temperature of the desuperheating pressure reducing steam and the preset expected temperature in the control device and adjusts the first electric water supply valve and the second electric water supply valve. The utility model discloses when satisfying the requirement of reducing temperature and pressure steam, more can regulate and control according to different temperature requirements in winter and summer, application scope is wide, uses portably.

Description

Steam temperature and pressure reduction adjusting system
Technical Field
The utility model relates to a chemical machinery technical field, in particular to steam temperature and pressure reduction technical field specifically indicates a steam temperature and pressure reduction governing system.
Background
High-temperature and high-pressure steam is often generated in the industrial production process, and the steam cannot be directly used due to the limitation of pressure and temperature, so that the steam is wasted in many occasions, and an extremely serious condition or even an accident occurs. Through using the steam temperature and pressure reduction device, the high-temperature and high-pressure steam can be reduced in temperature and pressure to a state suitable for other equipment, the steam recovery rate is improved, and the excessive waste of resources is avoided.
Steam temperature and pressure reduction devices are common in chemical engineering projects, electric power engineering and industrial plants, but generally, the devices only perform single temperature and pressure reduction on steam, for example, a steam temperature and pressure reduction device is disclosed in chinese utility model patent ZL201120067972.4, high-temperature and high-pressure steam sequentially enters a steam mixer through a steam inlet valve, a steam pressure reduction regulating valve and a steam valve; cooling water enters the steam mixer through the inlet flange ball valve, the cooling water regulating valve and the check valve, and steam and the cooling water are mixed in the steam mixer and then output to a steam using point through the outlet of the mixer. The device controls steam decompression governing valve and cooling water governing valve respectively through pressure and temperature after the decompression to make high temperature high pressure steam decompression to the steam that is fit for using, nevertheless the device is comparatively simple, can't regulate and control according to different temperature requirements in winter and summer.
Therefore, it is desirable to provide a steam temperature and pressure reducing regulation system, which can meet the requirements of steam temperature and pressure reduction, can be regulated and controlled according to different temperature requirements in winter and summer, and has wide application range and simple and convenient use.
SUMMERY OF THE UTILITY MODEL
In order to overcome the shortcoming among the above-mentioned prior art, an object of the utility model is to provide a steam temperature and pressure reduction governing system, it when satisfying steam temperature and pressure reduction requirement, more can regulate and control according to different temperature requirements in winter and summer, and application scope is wide, and convenience simple to use is suitable for extensive popularization and application.
Another object of the utility model is to provide a steam temperature and pressure reduction governing system, its design benefit, the structure is succinct, makes portably, low in manufacturing cost is suitable for extensive popularization and application.
In order to achieve the above object, the utility model provides a steam temperature and pressure reduction governing system, advance pipe, first electric pressure reducing valve, temperature and pressure reducer, steam exit tube, first pressure sensor, first temperature sensor, temperature reduction water source, first electronic feed water valve and controlling means including steam source, steam, the steam source passes through steam advances the pipe coupling first electric pressure reducing valve, first electric pressure reducing valve passes through temperature reduction pipe coupling the steam exit tube, first pressure sensor with first temperature sensor all sets up be used for measuring respectively in the steam exit tube the pressure and the temperature of temperature reduction pressure reduction steam in the steam exit tube, first pressure sensor with first temperature sensor difference signal connection controlling means be used for respectively with the pressure of temperature reduction pressure reduction steam with the temperature of temperature reduction pressure reduction steam send to controlling means, its characteristics are that steam temperature reduction and pressure reduction governing system still includes second pressure sensor, second temperature sensor, first electric gate valve, second electric gate valve, first temperature reduction water conveyor, second temperature reduction water supply water valve, second atomizing nozzle, wherein electric spray nozzle:
the steam inlet pipe is connected with the first electric pressure reducing valve through the first electric gate valve pipeline, the first electric pressure reducing valve is connected with the temperature and pressure reducing device through the second electric gate valve pipeline, the second pressure sensor and the second temperature sensor are arranged in the steam inlet pipe and used for measuring the pressure and the temperature of high-temperature and high-pressure steam in the steam inlet pipe respectively, the second pressure sensor and the second temperature sensor are connected with the control device through signals respectively and used for sending the pressure of the high-temperature and high-pressure steam and the temperature of the high-temperature and high-pressure steam to the control device respectively, and the control device is connected with the first electric gate valve, the first electric pressure reducing valve and the second electric gate valve through signals and used for adjusting the first electric gate valve, the first electric water feeding valve and the second electric gate valve according to the pressure of the high-temperature and high-pressure steam, the pressure of the temperature and pressure reducing steam and expected pressure preset in the control device respectively;
the temperature-reducing water source is respectively connected with the first electric water feeding valve and the second electric water feeding valve through the first temperature-reducing water conveying device in a pipeline mode, the temperature-reducing water source is further respectively connected with the first electric water feeding valve and the second electric water feeding valve through the second temperature-reducing water conveying device in a pipeline mode, the first atomizing nozzle and the second atomizing nozzle are inserted into the temperature-reducing pressure reducer, the nozzle head of the first atomizing nozzle and the nozzle head of the second atomizing nozzle are located in the temperature-reducing pressure reducer, the first electric water feeding valve and the second electric water feeding valve are respectively connected with the first atomizing nozzle and the second atomizing nozzle in a pipeline mode, the control device is further connected with the first temperature-reducing water conveying device, the second temperature-reducing water conveying device, the first electric water feeding valve and the second electric water feeding valve in a signal mode and used for opening and closing the first temperature-reducing water conveying device, opening and closing the second temperature-reducing water conveying device, adjusting the first electric water feeding valve and the second electric water feeding valve according to the temperature of the high-temperature-reducing high-pressure steam, the temperature-reducing steam and the expected temperature-reducing pressure steam preset in the control device.
Preferably, the first desuperheating water conveying device and the second desuperheating water conveying device are both water pumps.
Preferably, the steam temperature and pressure reduction regulating system further comprises a third electric gate valve, a second electric pressure reducing valve and a fourth electric gate valve, the steam inlet pipe is further connected with the second electric pressure reducing valve through a third electric gate valve pipeline, the second electric pressure reducing valve is connected with the temperature and pressure reducing device through a fourth electric gate valve pipeline, and the control device is further connected with the third electric gate valve, the second electric pressure reducing valve and the fourth electric gate valve through signals, and is used for regulating the third electric gate valve, the second electric pressure reducing valve and the fourth electric gate valve respectively according to the pressure of the high-temperature high-pressure steam, the pressure of the temperature and pressure reducing steam and the expected pressure preset in the control device when the first electric gate valve, the first electric pressure reducing valve or the second electric gate valve fails.
Preferably, the steam temperature and pressure reducing and regulating system further comprises a safety valve, and the safety valve is arranged on the temperature and pressure reducing device.
Preferably, the steam temperature and pressure reduction adjusting system further comprises a third temperature and pressure reduction water conveying device, the temperature reduction water source is further connected with the first electric water feed valve and the second electric water feed valve through the third temperature and pressure reduction water conveying device through pipelines respectively, and the control device is further connected with the third temperature and pressure reduction water conveying device through signals and used for opening and closing the third temperature and pressure reduction water conveying device according to the temperature of the high-temperature high-pressure steam, the temperature of the temperature and pressure reduction steam and the preset expected temperature in the control device when the first temperature and pressure reduction water conveying device or the second temperature and pressure reduction water conveying device breaks down.
Preferably, the steam temperature and pressure reduction adjusting system further comprises a first water pipe and a first manual control valve, the first manual control valve is arranged in the first water pipe, and the first temperature reduction water conveying device and the second temperature reduction water conveying device are both connected with the first atomizing nozzle through the first water pipe.
Preferably, the steam temperature and pressure reduction adjusting system further comprises a second water conveying pipeline and a second manual control valve, the second manual control valve is arranged in the second water conveying pipeline, and the first desuperheating water conveying device and the second desuperheating water conveying device are both connected with the second atomizing nozzle through a second water conveying pipeline.
Preferably, the steam temperature and pressure reducing and adjusting system further comprises a return water adjusting valve, an outdoor condensation water tank and a third pressure sensor, the first desuperheating water conveying device and the second desuperheating water conveying device are both connected with the outdoor condensation water tank through the return water adjusting valve, the third pressure sensor is arranged in a connecting pipeline which is located at the downstream of the first desuperheating water conveying device and the second desuperheating water conveying device and at the upstream of the first electric water feeding valve and the second electric water feeding valve and used for detecting the pressure in the connecting pipeline, the third pressure sensor is in signal connection with the control device and used for sending the pressure in the connecting pipeline to the control device, and the control device is further in signal connection with the return water adjusting valve and used for controlling the opening and closing of the return water adjusting valve according to the pressure in the connecting pipeline and the pipeline pressure preset in the control device.
Preferably, the steam temperature and pressure reduction adjusting system further comprises a steam filter, and the steam filter is arranged in the steam inlet pipe.
Preferably, the steam temperature and pressure reduction adjusting system further comprises a first temperature reduction water filter and a second temperature reduction water filter, the temperature reduction water source is connected with the first temperature reduction water conveying device through the first temperature reduction water filter pipeline, and the temperature reduction water source is connected with the second temperature reduction water conveying device through the second temperature reduction water filter pipeline.
The beneficial effects of the utility model mainly lie in:
1. the steam inlet pipe of the steam temperature and pressure reducing adjusting system of the utility model is connected with the steam outlet pipe through the first electric gate valve, the first electric pressure reducing valve, the second electric gate valve and the temperature and pressure reducing device pipeline in turn, and the control device respectively adjusts the first and the second electric gate valves and the first electric water feeding valve according to the pressure of high-temperature high-pressure steam, the pressure of temperature and pressure reducing steam and the expected pressure; the desuperheating water source is equallyd divide through first and second desuperheating water conveyor and divide difference tube coupling first and second electronic water feed valve, first and second electronic water feed valve respectively the first and second atomizing nozzle of tube coupling grafting in the desuperheating pressure reducer, controlling means is according to the temperature of high temperature high pressure steam, first and second desuperheating water conveyor is opened and close to the temperature of desuperheating pressure reducing steam and the expectation temperature of predetermineeing in controlling means, adjust first and second electronic water feed valve, therefore, it is when satisfying the requirement of reducing the temperature and pressure to steam, more can regulate and control according to different temperature requirements in winter and summer, application scope is wide, and is simple and convenient to use, and is suitable for extensive popularization and application.
2. The steam inlet pipe of the steam temperature and pressure reducing adjusting system of the utility model is connected with the steam outlet pipe through the first electric gate valve, the first electric pressure reducing valve, the second electric gate valve and the temperature and pressure reducing device pipeline in turn, and the control device respectively adjusts the first and the second electric gate valves and the first electric water feeding valve according to the pressure of high-temperature high-pressure steam, the pressure of temperature and pressure reducing steam and the expected pressure; the desuperheating water source is divided equally through first and second desuperheating water conveyor and is divided the first and second electronic water feed valve of difference tube coupling, first and second atomizing nozzle of pegging graft in the desuperheating pressure reducer is divided to first and second electronic water feed valve, controlling means is according to the temperature of high temperature high pressure steam, first and second desuperheating water conveyor is opened and close to the temperature of desuperheating pressure reducing steam and the anticipated temperature of predetermineeing in the controlling means, adjust first and second electronic water feed valve, therefore, its design benefit, the structure is succinct, it is simple and convenient to manufacture, low in manufacturing cost, be suitable for extensive popularization and application.
These and other objects, features and advantages of the present invention will become more fully apparent from the following detailed description and appended claims, or may be learned by the practice of the invention as set forth hereinafter.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the steam temperature and pressure reduction adjusting system of the present invention.
(symbol description)
1, steam inlet pipe; 2 a first electrically operated pressure reducing valve; 3, temperature and pressure reduction; 4, a steam outlet pipe; 5 a first pressure sensor; 6 a first temperature sensor; 7 a first electric water feed valve; 8 a control device; 9 a second pressure sensor; 10 a second temperature sensor; 11 a first electric gate valve; 12 a second electric gate valve; 13 a first desuperheating water conveying device; 14 a second desuperheating water conveying device; 15 a second electric water feed valve; 16 a first atomizing nozzle; 17 a second atomizing nozzle; 18 a third electric gate valve; 19 a second electrically operated pressure reducing valve; 20 a fourth electric gate valve; 21 a safety valve; 22 a third desuperheating water delivery device; 23 a first water conveying pipeline; 24 a second water conveying pipeline; 25 return water regulating valve; 26 a vapor filter; 27 a first desuperheating water filter; 28 a second desuperheating water filter; 29 a third desuperheating water filter; 30 a first manual control valve; 31 a second manual control valve; 32 outdoor condensation water tank; 33 third pressure sensor.
Detailed Description
In order to clearly understand the technical contents of the present invention, the following embodiments are specifically illustrated in detail.
In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being 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.
Please refer to fig. 1, in an embodiment of the present invention, the steam temperature and pressure reduction adjusting system includes a steam source (not shown in the figure), a steam inlet pipe 1, a first electric pressure reducing valve 2, a temperature and pressure reducing device 3, a steam outlet pipe 4, a first pressure sensor 5, a first temperature sensor 6, a temperature reducing water source (not shown in the figure), a first electric water feeding valve 7, a control device 8, a second pressure sensor 9, a second temperature sensor 10, a first electric gate valve 11, a second electric gate valve 12, a first temperature reducing water conveying device 13, a second temperature reducing water conveying device 14, a second electric water feeding valve 15, a first atomizing nozzle 16 and a second atomizing nozzle 17, wherein:
the steam source is connected with the first electric pressure reducing valve 2 through the steam inlet pipe 1 through a pipeline, the first electric pressure reducing valve 2 is connected with the steam outlet pipe 4 through the temperature and pressure reducing device 3 through a pipeline, the first pressure sensor 5 and the first temperature sensor 6 are both arranged in the steam outlet pipe 4 and used for measuring the pressure and the temperature of the temperature and pressure reducing steam in the steam outlet pipe 4 respectively, and the first pressure sensor 5 and the first temperature sensor 6 are respectively in signal connection with the control device 8 and used for sending the pressure of the temperature and pressure reducing steam and the temperature of the temperature and pressure reducing steam to the control device 8 respectively;
the steam inlet pipe 1 is connected with the first electric pressure reducing valve 2 through a first electric gate valve 11 by a pipeline, the first electric pressure reducing valve 2 is connected with the temperature and pressure reducing device 3 through a second electric gate valve 12 by a pipeline, the second pressure sensor 9 and the second temperature sensor 10 are both arranged in the steam inlet pipe 1 and are used for respectively measuring the pressure and the temperature of high-temperature and high-pressure steam in the steam inlet pipe 1, the second pressure sensor 9 and the second temperature sensor 10 are respectively in signal connection with the control device 8 and are used for respectively sending the pressure of the high-temperature and high-pressure steam and the temperature of the high-temperature and high-pressure steam to the control device 8, and the control device 8 is in signal connection with the first electric gate valve 11, the first electric pressure reducing valve 2 and the second electric gate valve 12 and is used for respectively adjusting the first electric gate valve 11, the first electric water feeding valve 7 and the second electric gate valve 12 according to the pressure of the high-temperature and high-pressure steam, the pressure reducing steam and the expected pressure preset pressure in the control device 8;
the desuperheating water source is respectively connected with the first electric water feeding valve 7 and the second electric water feeding valve 15 through the first desuperheating water conveying device 13, the desuperheating water source is also respectively connected with the first electric water feeding valve 7 and the second electric water feeding valve 15 through the second desuperheating water conveying device 14 through pipelines, the first atomizing nozzle 16 and the second atomizing nozzle 17 are inserted into the desuperheating pressure reducer 3, a nozzle head of the first atomizing nozzle 16 and a nozzle head of the second atomizing nozzle 17 are both positioned in the desuperheating pressure reducer 3, the first electric water feeding valve 7 and the second electric water feeding valve 15 are respectively connected with the first atomizing nozzle 16 and the second atomizing nozzle 17 through pipelines, the control device 8 is further in signal connection with the first desuperheating water conveying device 13, the second desuperheating water conveying device 14, the first electric water feeding valve 7 and the second electric water feeding valve 15, and is used for adjusting the opening and closing of the second electric water feeding valve 7 and the second electric water feeding valve 15 according to the temperature of the high-temperature high-pressure steam, the temperature of the desuperheating water and the desired temperature of the desuperheating control device 8.
The first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 can be any suitable water conveying device, and in a specific embodiment of the present invention, the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 are water pumps.
The steam temperature and pressure reducing adjusting system may further include any other suitable components, as shown in fig. 1, in a specific embodiment of the present invention, the steam temperature and pressure reducing adjusting system further includes a third electric gate valve 18, a second electric pressure reducing valve 19 and a fourth electric gate valve 20, the steam inlet pipe 1 is further connected to the second electric pressure reducing valve 19 through the third electric gate valve 18, the second electric pressure reducing valve 19 is connected to the temperature and pressure reducing device 3 through the fourth electric gate valve 20, and the control device 8 is further connected to the third electric gate valve 18, the second electric pressure reducing valve 19 and the fourth electric gate valve 20 in a signal manner, and is configured to respectively adjust the third electric gate valve 18, the second electric pressure reducing valve 19 and the fourth electric gate valve 20 according to the pressure of the high-temperature high-pressure steam, the pressure of the temperature and pressure reducing steam and the expected pressure preset in the control device 8 when the first electric gate valve 11, the first electric pressure reducing valve 2 or the second electric gate valve 12 fails.
Adopt above-mentioned setting, with third electric gate valve 18 second electric pressure reducing valve 19 with fourth electric gate valve 20 is as first electric gate valve 11 first electric pressure reducing valve 2 with the spare part of second electric gate valve 12 first electric gate valve 11 first electric pressure reducing valve 2 with during arbitrary one trouble in the second electric gate valve 12, adopt third electric gate valve 18 second electric pressure reducing valve 19 with fourth electric gate valve 20 replaces first electric gate valve 11 first electric pressure reducing valve 2 with second electric gate valve 12, play respectively with first electric gate valve 11 first electric pressure reducing valve 2 with the same effect of second electric gate valve 12.
The steam temperature and pressure reducing regulation system may also include any other suitable components, as shown in fig. 1, and in a specific embodiment of the present invention, the steam temperature and pressure reducing regulation system further includes a safety valve 21, and the safety valve 21 is disposed on the temperature and pressure reducing device 3.
The steam temperature and pressure reducing adjusting system may further include any other suitable components, please refer to fig. 1, in a specific embodiment of the present invention, the steam temperature and pressure reducing adjusting system further includes a third desuperheating water conveying device 22, the desuperheating water source further includes a pipeline connected to the first electric water feed valve 7 and the second electric water feed valve 15 through the third desuperheating water conveying device 22, the control device 8 further signal-connects the third desuperheating water conveying device 22 for opening and closing the third desuperheating water conveying device 22 according to the temperature of the high-temperature and high-pressure steam, the temperature of the desuperheating and pressure reducing steam and the desired temperature preset in the control device 8 when the first desuperheating water conveying device 13 or the second desuperheating water conveying device 14 fails.
With the above arrangement, the third desuperheating water conveying device 22 is used as a backup device for the first desuperheating water conveying device 13 or the second desuperheating water conveying device 14, and when any one of the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 fails, the third desuperheating water conveying device 22 is used to replace the failed device, and the same function as the failed device is achieved.
The third desuperheating water delivery device 22 may be any suitable water delivery device, and in an embodiment of the present invention, the third desuperheating water delivery device 22 is a water pump.
The steam temperature and pressure reducing adjusting system may further include any other suitable components, as shown in fig. 1, in a specific embodiment of the present invention, the steam temperature and pressure reducing adjusting system further includes a first water pipe 23 and a first manual control valve 30, the first manual control valve 30 is disposed in the first water pipe 23, and the first temperature reduced water delivery device 13 and the second temperature reduced water delivery device 14 are both connected to the first atomizing nozzle 16 through the first water pipe 23. In the case that the steam temperature and pressure reduction adjusting system further includes a third temperature reduction water delivery device 22, the third temperature reduction water delivery device 22 is connected to the first atomizing nozzle 16 through the first water pipe 23. The first water pipe 23 is a manual standby bypass of the first electric water supply valve 7, and when the first electric water supply valve 7 fails, the first manual control valve 30 is opened and closed manually to adjust the on-off of the first water pipe 23.
The steam temperature and pressure reducing adjusting system may further include any other suitable components, as shown in fig. 1, in a specific embodiment of the present invention, the steam temperature and pressure reducing adjusting system further includes a second water pipe 24 and a second manual control valve 31, the second manual control valve 31 is disposed in the second water pipe 24, and the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 are both connected to the second atomizing nozzle 17 through the second water pipe 24. In the case that the steam temperature and pressure reduction adjusting system further comprises a third desuperheating water conveying device 22, the third desuperheating water conveying device 22 is connected with the second atomizing nozzle 17 through the second water conveying pipeline 24. The second water pipe 24 is a manual standby bypass of the second electric water-feeding valve 15, and the second electric water-feeding valve 15 is opened or closed manually when the second electric water-feeding valve 15 fails, so that the second water pipe 24 is bypassed.
The steam temperature and pressure reducing and regulating system may further include any other suitable components, as shown in fig. 1, in a specific embodiment of the present invention, the steam temperature and pressure reducing and regulating system further includes a return water regulating valve 25, an outdoor condensed water tank 32 and a third pressure sensor 33, the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 are both connected to the outdoor condensed water tank 32 through the return water regulating valve 25, the third pressure sensor 33 is disposed in a connecting pipeline located downstream of the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 and upstream of the first electric water-feeding valve 7 and the second electric water-feeding valve 15 for detecting the pressure in the connecting pipeline, the third pressure sensor 33 is in signal connection with the control device 8 for sending the pressure in the connecting pipeline to the control device 8, and the control device 8 is further in signal connection with the return water regulating valve 25 for controlling the opening and closing of the return water regulating valve 25 according to the pressure in the connecting pipeline and the preset pipeline pressure in the control device 8. The preset pipeline pressure in the control device 8 is set according to the expected pipeline pressure, and by adopting the above setting, when the water flow conveyed by the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 cannot be consumed, namely, the pressure in the connecting pipeline detected by the third pressure sensor 33 exceeds the preset pipeline pressure, the control device 8 controls the return water regulating valve 25 to be opened, and the excess water is discharged to the outdoor condensed water tank 32. Under the condition that the steam temperature and pressure reduction adjusting system further comprises a third desuperheating water conveying device 22, the connecting pipeline is further located at the downstream of the third desuperheating water conveying device 22, and the third desuperheating water conveying device 22 is connected with the outdoor condensation water tank 32 through the return water adjusting valve 25.
The steam temperature and pressure reducing system may also include any other suitable components, as shown in fig. 1, and in an embodiment of the present invention, the steam temperature and pressure reducing system further includes a steam filter 26, and the steam filter 26 is disposed in the steam inlet pipe 1.
The steam temperature and pressure reducing adjusting system may further include any other suitable components, as shown in fig. 1, in a specific embodiment of the present invention, the steam temperature and pressure reducing adjusting system further includes a first temperature reducing water filter 27 and a second temperature reducing water filter 28, the temperature reducing water source is connected to the first temperature reducing water delivery device 13 through the first temperature reducing water filter 27, and the temperature reducing water source is connected to the second temperature reducing water delivery device 14 through the second temperature reducing water filter 28. Under the condition that the steam temperature and pressure reduction adjusting system further comprises a third temperature and pressure reduction water conveying device 22, the steam temperature and pressure reduction adjusting system further comprises a third temperature and pressure reduction water filter 29, and the temperature reduction water source is connected with the third temperature and pressure reduction water conveying device 22 through a third temperature and pressure reduction water filter 29 pipeline.
When the steam-water reducing device is used, a steam source is taken as a municipal steam pipe network, a temperature-reducing water source is taken as a municipal tap water pipe network as an example, high-temperature and high-pressure steam from the municipal steam pipe network enters the steam inlet pipe 1, the pressure and the temperature of the high-temperature and high-pressure steam are measured by the second pressure sensor 9 and the second temperature sensor 10, the high-temperature and high-pressure steam enters the first electric pressure reducing valve 2 through the first electric gate valve 11, is reduced in pressure by the first electric pressure reducing valve 2 and then enters the temperature-reducing pressure reducer 3 through the second electric gate valve 12, and the temperature-reducing water (tap water) from the municipal tap water pipe network is conveyed to the first electric water-feeding valve 7 and the second electric water-feeding valve 15 through the water conveying devices (namely the first temperature-reducing water conveying device 13 and the second temperature-reducing water conveying device 14) and then is respectively conveyed to the first atomizing nozzle 16 and the second atomizing nozzle 17, so as to reduce the temperature and reduce the pressure of the high-temperature steam entering the temperature and pressure reducer 3, thereby obtaining the temperature and pressure-reducing steam, and discharging the temperature-reducing steam from the steam outlet pipe 4 for use by end equipment.
The following example is to reduce the temperature and pressure of high-temperature high-pressure steam with pressure of 1.5MPa and temperature of 220 ℃ from municipal steam pipe network to steam with pressure of 0.5MPa and temperature of 152 ℃ (which can be set according to the requirements of end users and equipment in summer and winter), and the pressure and temperature regulation process of the present invention is adopted:
pressure regulation:
the preset expected pressure in the control device 8 is 0.5MPa, when high-temperature high-pressure steam passes through the second pressure sensor 9, the second pressure sensor 9 detects that the pressure of the high-temperature high-pressure steam is 1.5MPa, the second pressure sensor 9 sends the pressure of the high-temperature high-pressure steam to the control device 8, the control device 8 compares the pressure of the high-temperature high-pressure steam with the preset expected pressure to control the first electric pressure reducing valve 2 to reduce the pressure, the pressure reduction amplitude is realized by controlling the first electric gate valve 11 through the control device 8, the control device 8 controls the second electric gate valve 12 to be normally open and not to act in a normal operation state, the first pressure sensor 5 detects the actual pressure of the temperature and pressure reducing steam and sends the actual pressure of the temperature and pressure reducing steam to the control device 8, if the actual pressure of the temperature and pressure reducing steam is higher than the preset expected pressure, the control device 8 controls the first electric pressure reducing valve 2 and the first electric gate valve 11 to further reduce the pressure, and if the actual pressure of the temperature and pressure reducing steam is lower than the preset expected pressure, and the pressure reducing degree of the first electric gate valve 2 and the first electric gate valve 11. When the first electric pressure reducing valve 2 is in fault and needs to be overhauled, the control device 8 controls the first electric gate valve 11 and the second electric gate valve 12 to be closed to cut off steam, and therefore overhauling safety is guaranteed.
Temperature regulation:
the preset expected temperature in the control device 8 is 152 ℃, when high-temperature high-pressure steam passes through the second temperature sensor 10, the second temperature sensor 10 detects that the temperature of the high-temperature high-pressure steam is 220 ℃, the second temperature sensor 10 sends the temperature of the high-temperature high-pressure steam to the control device 8, the control device 8 compares the temperature of the high-temperature high-pressure steam with the preset expected temperature to control the first desuperheating water conveying device 13 and the second desuperheating water conveying device 14 to start, controls the first electric water feeding valve 7 to open, sprays desuperheating water through the first atomizing nozzle 16 to cool, detects the actual temperature of the desuperheating and depressurizing steam through the first temperature sensor 6 and sends the actual temperature of the desuperheating and depressurizing steam to the control device 8, and if the actual temperature of the desuperheating and depressurizing steam is higher than the preset expected temperature, the control device 8 controls the first electric water feeding valve 7 to adjust the valve opening degree of the first electric water feeding valve 7 to be larger, so that the desuperheating amplitude is controlled. The second electronic feed valve 15 normal close of connecting second atomizing nozzle 17 under the normal operating condition does not move, and it is lower to require when the terminal service temperature in summer, and preset expectation temperature is lower promptly, and when first electronic feed valve 7 desuperheating can't satisfy the requirement, control second electronic feed valve 15 by controlling means 8 and open, spray the cooling water cooling through second atomizing nozzle 17, spray the cooling water together through second atomizing nozzle 17 promptly and second atomizing nozzle 16 and 17 and reduce steam temperature and satisfy end user's practical demand.
Therefore, adopt the utility model discloses, can not only reach the temperature and pressure reduction effect of temperature and pressure reduction device to steam in the past, more can regulate and control and switch the steam demand in different operating modes in winter and summer, intelligent control degree is higher moreover, more can reduce the on-the-spot manual work load that plays to close the switching valve of operating personnel, has effectively reduced personnel site operation's safe risk.
To sum up, the utility model discloses a steam temperature and pressure reduction governing system more can regulate and control according to different temperature requirements in winter and summer when satisfying the requirement to steam temperature and pressure reduction, and application scope is wide, and simple to use is convenient, design benefit, and the structure is succinct, makes portably, and low in manufacturing cost is suitable for extensive popularization and application.
Therefore, the purpose of the utility model is completely and effectively realized. The functional and structural principles of the present invention have been shown and described in the embodiments, and the embodiments may be modified without departing from the principles. Therefore, this invention includes all modifications encompassed within the spirit and scope of the claims.

Claims (10)

1. The utility model provides a steam temperature and pressure reduction governing system, includes that steam source, steam advance tub, first electronic relief pressure valve, temperature reduction pressure reducer, steam exit tube, first pressure sensor, first temperature sensor, temperature reduction water source, first electronic water feed valve and controlling means, the steam source passes through steam advances a pipe coupling first electronic relief pressure valve, first electronic relief pressure valve passes through temperature reduction pressure reducer pipe coupling the steam exit tube, first pressure sensor with first temperature sensor all sets up be used for measuring respectively in the steam exit tube the pressure and the temperature of temperature reduction pressure reduction steam in the steam exit tube, first pressure sensor with first temperature sensor difference signal connection controlling means be used for respectively with the pressure of temperature reduction pressure reduction steam with the temperature of temperature reduction pressure reduction steam send to controlling means, its characterized in that, steam temperature reduction and pressure reduction governing system still includes second pressure sensor, second temperature sensor, first electronic gate valve, second electronic gate valve, first electronic warm water conveyor, second temperature reduction water feed valve, second electronic spray nozzle, wherein atomizing nozzle:
the steam inlet pipe is connected with the first electric pressure reducing valve through the first electric gate valve pipeline, the first electric pressure reducing valve is connected with the temperature and pressure reducing device through the second electric gate valve pipeline, the second pressure sensor and the second temperature sensor are arranged in the steam inlet pipe and used for measuring the pressure and the temperature of high-temperature and high-pressure steam in the steam inlet pipe respectively, the second pressure sensor and the second temperature sensor are connected with the control device through signals respectively and used for sending the pressure of the high-temperature and high-pressure steam and the temperature of the high-temperature and high-pressure steam to the control device respectively, and the control device is connected with the first electric gate valve, the first electric pressure reducing valve and the second electric gate valve through signals and used for adjusting the first electric gate valve, the first electric water feeding valve and the second electric gate valve according to the pressure of the high-temperature and high-pressure steam, the pressure of the temperature and pressure reducing steam and expected pressure preset in the control device respectively;
the temperature-reducing water source is respectively connected with the first electric water supply valve and the second electric water supply valve through the first temperature-reducing water conveying device in a pipeline mode, the temperature-reducing water source is further respectively connected with the first electric water supply valve and the second electric water supply valve through the second temperature-reducing water conveying device in a pipeline mode, the first atomizing nozzle and the second atomizing nozzle are inserted into the temperature-reducing pressure reducer, the nozzle head of the first atomizing nozzle and the nozzle head of the second atomizing nozzle are located in the temperature-reducing pressure reducer, the first electric water supply valve and the second electric water supply valve are respectively connected with the first atomizing nozzle and the second atomizing nozzle in a pipeline mode, and the control device is further connected with the first temperature-reducing water conveying device, the second temperature-reducing water conveying device, the first electric water supply valve and the second electric water supply valve in a signal mode and used for opening and closing the first temperature-reducing water conveying device, opening and closing the second temperature-reducing water conveying device, adjusting the first electric water supply valve and the second electric water supply valve according to the temperature of the high-temperature-high-temperature high-pressure steam, the temperature-reducing water steam and the expected temperature-reducing pressure steam preset in the control device.
2. A steam desuperheating and pressure reducing regulation system as claimed in claim 1 wherein said first desuperheating water delivery means and said second desuperheating water delivery means are both water pumps.
3. A steam temperature and pressure reducing regulating system as claimed in claim 1, further comprising a third electric gate valve, a second electric pressure reducing valve and a fourth electric gate valve, wherein the steam inlet pipe is further connected to the second electric pressure reducing valve through a third electric gate valve, the second electric pressure reducing valve is connected to the temperature and pressure reducing valve through a fourth electric gate valve, and the control device is further connected to the third electric gate valve, the second electric pressure reducing valve and the fourth electric gate valve in signal mode for respectively regulating the third electric gate valve, the second electric pressure reducing valve and the fourth electric gate valve according to the pressure of the high-temperature high-pressure steam, the pressure of the temperature and pressure reducing steam and a desired pressure preset in the control device when the first electric gate valve, the first electric pressure reducing valve or the second electric gate valve fails.
4. The steam attemperation and depressurization regulation system of claim 1 further comprising a safety valve disposed on the attemperation and depressurization regulator.
5. The steam temperature and pressure reducing and adjusting system according to claim 1, further comprising a third temperature and pressure reducing water delivery device, wherein the temperature reducing water source is further connected with the first electric water feeding valve and the second electric water feeding valve through the third temperature and pressure reducing water delivery device by pipelines, and the control device is further connected with the third temperature and pressure reducing water delivery device by signals and is used for opening and closing the third temperature and pressure reducing water delivery device according to the temperature of the high-temperature high-pressure steam, the temperature of the temperature and pressure reducing steam and a preset expected temperature in the control device when the first temperature and pressure reducing water delivery device or the second temperature and pressure reducing water delivery device fails.
6. A steam temperature and pressure reducing adjusting system according to claim 1, further comprising a first water pipe and a first manual control valve, wherein the first manual control valve is disposed in the first water pipe, and the first desuperheating water delivery device and the second desuperheating water delivery device are both connected to the first atomizing nozzle through the first water pipe.
7. A steam temperature and pressure reducing adjusting system as recited in claim 1, further comprising a second water pipe and a second manual control valve, wherein the second manual control valve is disposed in the second water pipe, and both the first desuperheating water conveying device and the second desuperheating water conveying device are connected to the second atomizing nozzle through the second water pipe.
8. The steam temperature-reducing and pressure-reducing adjusting system according to claim 1, further comprising a return water adjusting valve, an outdoor condensation water tank, and a third pressure sensor, wherein the first temperature-reducing water conveying device and the second temperature-reducing water conveying device are both connected to the outdoor condensation water tank through the return water adjusting valve, the third pressure sensor is disposed in a connecting pipeline located at the downstream of the first temperature-reducing water conveying device and the second temperature-reducing water conveying device and located at the upstream of the first electric water-feeding valve and the second electric water-feeding valve and used for detecting the pressure in the connecting pipeline, the third pressure sensor is in signal connection with the control device and used for sending the pressure in the connecting pipeline to the control device, and the control device is further in signal connection with the return water adjusting valve and used for controlling the opening and closing of the return water adjusting valve according to the pressure in the connecting pipeline and the pipeline pressure preset in the control device.
9. The system of claim 1, further comprising a vapor filter disposed in the vapor inlet conduit.
10. The steam attemperation and pressure reduction system of claim 1, further comprising a first attemperation water filter and a second attemperation water filter, wherein the attemperation water source is connected to the first attemperation water delivery device through the first attemperation water filter pipeline, and wherein the attemperation water source is connected to the second attemperation water delivery device through the second attemperation water filter pipeline.
CN202222455771.2U 2022-09-16 2022-09-16 Steam temperature and pressure reduction adjusting system Active CN218001168U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202222455771.2U CN218001168U (en) 2022-09-16 2022-09-16 Steam temperature and pressure reduction adjusting system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202222455771.2U CN218001168U (en) 2022-09-16 2022-09-16 Steam temperature and pressure reduction adjusting system

Publications (1)

Publication Number Publication Date
CN218001168U true CN218001168U (en) 2022-12-09

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202222455771.2U Active CN218001168U (en) 2022-09-16 2022-09-16 Steam temperature and pressure reduction adjusting system

Country Status (1)

Country Link
CN (1) CN218001168U (en)

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