CN208059606U - A kind of pressure-controlled steam exhaust recovering device - Google Patents
A kind of pressure-controlled steam exhaust recovering device Download PDFInfo
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- CN208059606U CN208059606U CN201820560828.6U CN201820560828U CN208059606U CN 208059606 U CN208059606 U CN 208059606U CN 201820560828 U CN201820560828 U CN 201820560828U CN 208059606 U CN208059606 U CN 208059606U
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- steam exhaust
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- 239000007788 liquid Substances 0.000 claims abstract description 129
- 238000000926 separation method Methods 0.000 claims abstract description 104
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000001816 cooling Methods 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 238000009434 installation Methods 0.000 claims abstract description 4
- 238000009833 condensation Methods 0.000 claims description 7
- 230000005494 condensation Effects 0.000 claims description 7
- 238000004064 recycling Methods 0.000 abstract description 9
- 239000002699 waste material Substances 0.000 abstract description 9
- 230000001172 regenerating effect Effects 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 235000019628 coolness Nutrition 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of pressure-controlled steam exhaust recovering devices, are related to energy regenerating using technical field, which includes：Combine vapor-liquid separation component, steam exhaust circulating cooling component and the frequency conversion voltage controlled component of installation, condensed water and steam exhaust mixture enter in the vapor-liquid separation component, after vapor-liquid separation, the condensed water is sunk in the vapor-liquid separation component, the steam exhaust enters the steam exhaust circulating cooling component and carries out circulating cooling, and steam exhaust cold liquid after cooling is passed into the vapor-liquid separation component and is stored, the frequency conversion voltage controlled component adjusts the air-cooled load of the steam exhaust circulating cooling component according to the inside vapour phase pressure of the vapor-liquid separation component in real time.Structure setting is compact, realizes effective steam exhaust recycling and utilizes, and avoids the discharge of steam exhaust and the pollution of the waste and environment of high-quality water that generates.
Description
Technical field
The utility model is related to energy regeneratings to utilize technical field more particularly to a kind of pressure-controlled steam exhaust recovering device.
Background technology
In chemical industry application, for low-temperature heat source due to lacking suitable cold-trap, utility value is low, often relative surplus.
Technique productions device is using steam is to equipment and medium heating, heat tracing and stripping will produce a large amount of steam condensates and pressure is low
Steam（Commonly referred to as steam exhaust）, it is big using difficulty because of temperature, pressure or flow deficient in stability and certainty, and be not easy to find
Corresponding cold-trap is recycled, to the recycling of steam exhaust hinder device stability operation and safety in production, often do not repay
It loses, is forced direct emission, thus can cause the waste of the white pollution and high-quality water resource to surrounding enviroment again.
In realizing process of the present invention, inventor has found that at least there are the following problems in the prior art：
Traditional way is introduced into condensate-water polishing tank and carries out steam-water separation, and condensed water send to condensate polishing treatment and fills
It sets, makees boiler water-filling after processing is qualified, the exhaust steam straight of low pressure is connected on each spaced point and is directly put to idle discharge, causes high-grade water
Matter and contained thermal energy are not utilized rationally.
Invention content
In order to overcome the shortcomings of Related product in the prior art, the utility model proposes a kind of pressure-controlled steam exhaust recycling dresses
It sets, solves the problems, such as at present not efficiently using steam exhaust.
The utility model provides a kind of pressure-controlled steam exhaust recovering device, including：Vapor-liquid separation component, steam exhaust circulating cooling
Component and frequency conversion voltage controlled component；
The vapor-liquid separation component, steam exhaust circulating cooling component and the combination installation of frequency conversion voltage controlled component, condensed water and weary
Vapour mixture enters in the vapor-liquid separation component, and after vapor-liquid separation, the condensed water sinks to the vapor-liquid separation component
Interior, the steam exhaust enters the steam exhaust circulating cooling component and carries out circulating cooling, and steam exhaust cold liquid after cooling is passed into institute
Storage, the frequency conversion voltage controlled component in vapor-liquid separation component is stated to be adjusted in real time according to the inside vapour phase pressure of the vapor-liquid separation component
The air-cooled load of the whole steam exhaust circulating cooling component.
In some embodiments, the vapor-liquid separation component includes condensed water and steam exhaust inlet pipe, concetrated pipe and vapour-liquid
Knockout drum, the upper end of the concetrated pipe are connected to the condensed water and steam exhaust inlet pipe, the lower end of the concetrated pipe and the vapour-liquid
Knockout drum is connected to, and the vapor-liquid separation tank is connected to the steam exhaust circulating cooling component；Condensed water and steam exhaust mixture pass through institute
It states condensed water and steam exhaust inlet pipe enters the concetrated pipe, the condensed water and steam exhaust mixture are imported into institute by the concetrated pipe
It states in vapor-liquid separation tank, the condensed water is sunk in the vapor-liquid separation tank, and it is cold that the steam exhaust is then passed into the steam exhaust cycle
But in component.
In some embodiments, the vapor-liquid separation component further includes vapour phase around flowing plate, and the vapour phase is arranged around flowing plate
In the vapor-liquid separation tank.
In some embodiments, the vapor-liquid separation component further includes fluid-tight plate and condensate pump, the fluid-tight plate
Bottom end on the inside of the vapor-liquid separation tank is set, fluid-tight, the condensed water are cooperatively formed with the steam exhaust circulating cooling component
Pump is arranged outside the vapor-liquid separation tank, and the condensate pump is connected to the vapor-liquid separation tank, sinks to the vapour-liquid
Condensed water in knockout drum overflows the part of the fluid-tight plate, is extracted out and is sent to outside by the condensate pump.
In some embodiments, the vapor-liquid separation component is set between the condensate pump and the vapor-liquid separation tank
Liquid level adjusting valve and liquid level sensor are set, is detected in real time in the vapor-liquid separation tank by the liquid level sensor and overflows part
Condensed water water level, and automatically control the Liquid level adjusting valve to adjust the working condition of the condensate pump.
In some embodiments, height of the top of the fluid-tight plate away from the vapor-liquid separation pot bottom is 200~500
mm。
In some embodiments, the steam exhaust circulating cooling component include air cooler, de- vapour tank, the steam exhaust line of return and
Diversion pipe, the air cooler setting are connected to above the vapor-liquid separation tank, and by vapour phase pipeline with the vapor-liquid separation tank,
The de- vapour tank is connected to the other end of the air cooler, and the steam exhaust line of return is arranged in the air cooler and the de- vapour tank
Top, the both ends of the steam exhaust line of return are connected to the air cooler and the de- vapour tank respectively, the diversion pipe it is upper
End is connected to the bottom of the de- vapour tank, is connected to inside the lower end of the diversion pipe and the vapor-liquid separation tank.
In some embodiments, the diversion pipe and vertical direction are in 30 ° of predetermined angle.
In some embodiments, the frequency conversion voltage controlled component includes pressure sensor, frequency-variable controller and motor,
The motor is connect with the fan of the air cooler, and the pressure sensor is for detecting the vapor-liquid separation tank inner tip
Pressure, the frequency-variable controller controls the operation power of the motor according to the detection data of the pressure sensor, from
And accordingly adjust the live load of the air cooler.
Compared with prior art, the utility model has the advantage that：
Pressure-controlled steam exhaust recovering device described in the utility model embodiment is by the vapor-liquid separation component to condensed water
Vapor-liquid separation is carried out with steam exhaust mixture, the steam exhaust circulating cooling component carries out circulating cooling to steam exhaust, and steam exhaust is cooled down
Cold liquid afterwards is passed into storage in the vapor-liquid separation component, and the frequency conversion voltage controlled component is according in the vapor-liquid separation component
Portion's vapour phase pressure adjusts the air-cooled load of the steam exhaust circulating cooling component in real time, and structure setting is compact, realizes effective weary
Vapour is recycled and is utilized, and avoids the discharge of steam exhaust and the pollution of the waste and environment of high-quality water that generates, while change is utilized
Frequency voltage controlled component adjusts air-cooled load in real time, avoids the excessive condensation when recycling condensed water in high temperature and steam exhaust and wastes energy
Amount.
Description of the drawings
In order to illustrate more clearly of the technical scheme in the embodiment of the utility model, will make below to required in embodiment
Attached drawing is briefly described, it should be apparent that, the accompanying drawings in the following description is only some embodiments of the utility model,
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings
Other attached drawings.
Fig. 1 is the theory structure schematic diagram of pressure-controlled steam exhaust recovering device described in the utility model embodiment；
Reference sign：
1- vapor-liquid separations component, 2- steam exhaust circulating coolings component, 3- frequency conversions voltage controlled component, 11- condensed waters and steam exhaust inlet pipe,
12- concetrated pipes, 13- vapor-liquid separation tanks, 14- vapour phases are around flowing plate, 15- fluid-tights plate, 16- condensate pumps, 17- Liquid level adjusting valves, 18-
Liquid level sensor, 21- air coolers, 22- take off vapour tank, the 23- steam exhaust line of return, 24- diversion pipes, 31- pressure sensors, 32- frequency conversions
Controller, 33- motor.
Specific implementation mode
In order to make those skilled in the art more fully understand the utility model, below in conjunction with the utility model reality
The attached drawing in example is applied, technical scheme in the embodiment of the invention is clearly and completely described.Obviously, described implementation
Example be only the utility model a part of the embodiment, give instead of all the embodiments, in attached drawing the utility model compared with
Good embodiment.The utility model can be realized in many different forms, however it is not limited to embodiment described herein, on the contrary
Ground, purpose of providing these embodiments is makes the understanding of the disclosure of the utility model more thorough and comprehensive.Based on this reality
With the embodiment in novel, those of ordinary skill in the art are obtained every other without creative efforts
Embodiment shall fall within the protection scope of the present invention.
Unless otherwise defined, all of technologies and scientific terms used here by the article is led with the technology for belonging to the utility model
The normally understood meaning of technical staff in domain is identical.Term used in the description of the utility model is intended merely to describe
The purpose of specific embodiment, it is not intended that in limitation the utility model.The specification and claims of the utility model and
Term " comprising " and " having " in above-mentioned attached drawing and their any deformations, it is intended that cover and non-exclusive include.At this
" embodiment " is referred in text it is meant that a particular feature, structure, or characteristic described may be embodied in this practicality newly in conjunction with the embodiments
In at least one embodiment of type.The phrase, which occurs, in each position in the description might not each mean identical implementation
Example, nor the independent or alternative embodiment with other embodiments mutual exclusion.Those skilled in the art are explicitly and implicitly
Understand, embodiment described herein can be combined with other embodiments.
Fig. 1 is the theory structure schematic diagram of pressure-controlled steam exhaust recovering device described in the utility model embodiment, refering to fig. 1 institute
Show, the pressure-controlled steam exhaust recovering device includes vapor-liquid separation component 1, steam exhaust circulating cooling component 2 and frequency conversion voltage controlled component
3, the vapor-liquid separation component 1, steam exhaust circulating cooling component 2 and the combination installation of frequency conversion voltage controlled component 3, condensed water and steam exhaust are mixed
Object is closed to enter in the vapor-liquid separation component 1, after vapor-liquid separation, the condensed water is sunk in the steam-water separation component 1,
The steam exhaust enters the steam exhaust circulating cooling component 2 and carries out circulating cooling, and steam exhaust cold liquid after cooling is passed into described
Storage, the frequency conversion voltage controlled component 3 are real-time according to the inside vapour phase pressure of the vapor-liquid separation component 1 in vapor-liquid separation component 1
The air-cooled load of the steam exhaust circulating cooling component 2 is adjusted, structure setting is compact, realizes effective steam exhaust recycling, avoids
The discharge of steam exhaust and the pollution of the waste and environment of high-quality water generated, while frequency conversion voltage controlled component 3 is utilized and adjusts in real time
Whole air-cooled load avoids the excessive condensation when recycling condensed water in high temperature and steam exhaust and wastes energy.
The vapor-liquid separation component 1 includes condensed water and steam exhaust inlet pipe 11, concetrated pipe 12 and vapor-liquid separation tank 13, described
The upper end of concetrated pipe 12 is connected to the condensed water and steam exhaust inlet pipe 11, the lower end of the concetrated pipe 12 and the vapor-liquid separation tank
13 connections, the vapor-liquid separation tank 13 are connected to the steam exhaust circulating cooling component 2；Condensed water and steam exhaust mixture pass through described
Condensed water and steam exhaust inlet pipe 11 enter the concetrated pipe 12, and the concetrated pipe 12 imports the condensed water and steam exhaust mixture
Into the vapor-liquid separation tank 13, the condensed water is sunk in the vapor-liquid separation tank 13, and the steam exhaust is then passed into described weary
In vapour cycle cooling component 2.
In the utility model embodiment, when the vapor-liquid separation tank works normally, the pressure of inner tip is reachable
30KPa, the temperature of the vapor-liquid separation tank inner tip is up to 95 DEG C.
In some embodiments of the utility model, the vapor-liquid separation component 1 can also include vapour phase around flowing plate 14,
The vapour phase is arranged around flowing plate 14 in the vapor-liquid separation tank 13, can effectively strengthen vapor-liquid separation effect, avoids described
The more condensed water is carried in steam exhaust secretly, to reduce the live load of the steam exhaust circulating cooling component 2.
The vapor-liquid separation component 1 can also include fluid-tight plate 15 and condensate pump 16, and the setting of fluid-tight plate 15 exists
The bottom end of 13 inside of the vapor-liquid separation tank, fluid-tight, the top of the fluid-tight plate are cooperatively formed with the steam exhaust circulating cooling component 2
Height of the portion away from 13 bottom of the vapor-liquid separation tank is 200~500 mm, for example, it may be 300 mm etc., certainly, in this practicality
In novel other embodiment, the fluid-tight plate 15 can also be the structure of other congenerous, and overhead height can also be
Other numerical value, there is no restriction to this for the utility model；The condensate pump 16 is arranged outside the vapor-liquid separation tank 13, and
The condensate pump 16 is connected to the vapor-liquid separation tank 13, is sunk to described in the condensed water spilling in the vapor-liquid separation tank 13
The part of fluid-tight plate 15 is extracted out by the condensate pump 16 and is sent to external reasonable employment；The condensate pump 16 is using anti-
Cavitation type can be adapted for delivering up to 95 DEG C of condensed water in high temperature.
Certainly it should be noted that in the other embodiment of the utility model, the vapor-liquid separation component 1 can be with
Liquid level adjusting valve 17 and liquid level sensor 18 are set between the condensate pump 16 and the vapor-liquid separation tank 13, pass through institute
It states liquid level sensor 18 and detects the water level for the condensed water for overflowing part in the vapor-liquid separation tank 13 in real time, and automatically control described
Liquid level adjusting valve 17 is to adjust the working condition of the condensate pump 16.
The steam exhaust circulating cooling component 2 includes air cooler 21, takes off vapour tank 22, the steam exhaust line of return 23 and diversion pipe 24,
The setting of the air cooler 21 is connected to above the vapor-liquid separation tank 13, and by vapour phase pipeline with the vapor-liquid separation tank 13,
Convenient for collecting the steam exhaust risen, height of the air cooler 21 away from the vapor-liquid separation tank 13 is arranged according to actual demand, for example,
Can be 4m, 6m etc.；The de- vapour tank 22 is connected to the other end of the air cooler 21, and the steam exhaust line of return 23 is arranged in institute
State the top of air cooler 21 and the de- vapour tank 22, the both ends of the steam exhaust line of return 23 respectively with the air cooler 21 and institute
It states de- vapour tank 22 to be connected to, the upper end of the diversion pipe 24 is connected to the bottom of the de- vapour tank 22, the lower end of the diversion pipe 24
It is connected to 13 inside of the vapor-liquid separation tank, steam exhaust is condensed by the vapour phase pipeline into the air cooler 21, condensation
Cold liquid and uncooled steam exhaust afterwards enters in the de- vapour tank 22, and condensed cold liquid is by the diversion pipe 24 in gravity
It is imported under effect in the vapor-liquid separation tank 13, uncooled steam exhaust then rises and returns to institute by the steam exhaust line of return 23
It states air cooler 21 to continue to condense, repeats aforesaid operations until all steam exhaust condensations finish.
In the utility model embodiment, the diversion pipe 24 is in predetermined angle with vertical direction, after steam exhaust condensation
Cold liquid be flowed into the vapor-liquid separation tank 13, effectively prevent vapour locking and vapour phase during lower liquid to pass through the diversion pipe 24
Alter；For example, the predetermined angle can be 30 °, certainly, it should be noted that in practical work process, the water conservancy diversion
The angle that pipe 24 is arranged with vertical direction can be adjusted voluntarily according to actual demand, however it is not limited to and 30 °, in some possible implementations
It can also be 20 °, 40 ° etc., there is no restriction to this for the utility model in mode.
The frequency conversion voltage controlled component 3 includes pressure sensor 31, frequency-variable controller 32 and motor 33, the motor
33 connect with the fan of the air cooler 21, and provide power for the fan；The pressure sensor 31 is described for detecting
The pressure of 13 inner tip of vapor-liquid separation tank, the frequency-variable controller 32 are controlled according to the detection data of the pressure sensor 31
The operation power of the motor 33, to accordingly adjust the live load of the air cooler 21, the motor 33 is to described
The adjustable extent of 21 live load of air cooler is 0~100%, is effectively prevented excessive when recycling condensed water in high temperature and steam exhaust
It condenses and wastes energy.
Pressure-controlled steam exhaust recovering device described in the utility model embodiment is by the vapor-liquid separation component 1 to condensed water
Vapor-liquid separation is carried out with steam exhaust mixture, the steam exhaust circulating cooling component 2 to condensed water and steam exhaust mixture recycle cold
But it, and by steam exhaust cold liquid after cooling is passed into storage in the vapor-liquid separation component 1, the frequency conversion voltage controlled component 3 is according to institute
The inside vapour phase pressure for stating vapor-liquid separation component 1 adjusts the air-cooled load of the steam exhaust circulating cooling component 2, structure setting in real time
It is compact, it realizes effective steam exhaust recycling and utilizes, avoid the discharge of steam exhaust and the waste of high-quality water generated and environment
Pollution, while frequency conversion voltage controlled component 3 is utilized to adjust air-cooled load in real time, avoids in recycling condensed water in high temperature and weary
Excessive condensation when vapour and waste energy.
In above-described embodiment provided by the utility model, it should be understood that disclosed device, it can be by other
Mode realize.For example, the apparatus embodiments described above are merely exemplary, for example, the division of the module, only
For a kind of division of logic function, formula that in actual implementation, there may be another division manner, for example, multiple module or components can combine
Or it is desirably integrated into another system, or some features can be ignored or not executed.
The module or component illustrated as separating component may or may not be physically separated, as
The component that module or component is shown may or may not be physical module, can both be located at a place, or also may be used
To be distributed in multiple network element.Some or all of module or component therein can be selected according to the actual needs to come in fact
The purpose of existing this embodiment scheme.
It these are only the embodiments of the present invention, be not intended to limit the scope of the claims of the utility model, although with reference to before
Embodiment is stated the utility model is described in detail, it, still can be right for those skilled in the art comes
Technical solution recorded in aforementioned each specific implementation mode is modified, or carries out equivalent replace to which part technical characteristic
It changes.Every equivalent structure done using the utility model specification and accompanying drawing content is directly or indirectly used in other correlations
Technical field, similarly within the utility model patent protection domain.
Claims (9)
1. a kind of pressure-controlled steam exhaust recovering device, which is characterized in that including：Vapor-liquid separation component, steam exhaust circulating cooling component with
And frequency conversion voltage controlled component；
The vapor-liquid separation component, steam exhaust circulating cooling component and the combination installation of frequency conversion voltage controlled component, condensed water and steam exhaust are mixed
It closes object to enter in the vapor-liquid separation component, after vapor-liquid separation, the condensed water is sunk in the vapor-liquid separation component, institute
It states steam exhaust and carries out circulating cooling into the steam exhaust circulating cooling component, and steam exhaust cold liquid after cooling is passed into the vapour-liquid
It is stored in separation assembly, described in inside vapour phase pressure adjustment in real time of the frequency conversion voltage controlled component according to the vapor-liquid separation component
The air-cooled load of steam exhaust circulating cooling component.
2. pressure-controlled steam exhaust recovering device according to claim 1, it is characterised in that：The vapor-liquid separation component includes solidifying
It bears water and steam exhaust inlet pipe, concetrated pipe and vapor-liquid separation tank, the upper end of the concetrated pipe is connected to the steam exhaust inlet pipe, the collection
The lower end for closing pipe is connected to the vapor-liquid separation tank, and the vapor-liquid separation tank is connected to the steam exhaust circulating cooling component；Condensation
Water and steam exhaust mixture enter the concetrated pipe by the condensed water and steam exhaust inlet pipe, and the concetrated pipe is by the condensed water
And steam exhaust mixture is imported into the vapor-liquid separation tank, the condensed water is sunk in the vapor-liquid separation tank, and the steam exhaust is then
It is passed into the steam exhaust circulating cooling component.
3. pressure-controlled steam exhaust recovering device according to claim 2, it is characterised in that：The vapor-liquid separation component further includes
Vapour phase is arranged around flowing plate in the vapor-liquid separation tank around flowing plate, the vapour phase.
4. pressure-controlled steam exhaust recovering device according to claim 2, it is characterised in that：The vapor-liquid separation component further includes
The bottom end on the inside of the vapor-liquid separation tank is arranged in fluid-tight plate and condensate pump, the fluid-tight plate, is recycled with the steam exhaust cold
But component cooperatively forms fluid-tight, and the condensate pump is arranged outside the vapor-liquid separation tank, and the condensate pump with it is described
Vapor-liquid separation tank is connected to, and the condensed water sunk in the vapor-liquid separation tank overflows the part of the fluid-tight plate, by described solidifying
It bears water pumped and send to outside.
5. pressure-controlled steam exhaust recovering device according to claim 4, it is characterised in that：The vapor-liquid separation component is described
Liquid level adjusting valve and liquid level sensor are set between condensate pump and the vapor-liquid separation tank, pass through liquid level sensor reality
When detect the water level for the condensed water that part is overflowed in the vapor-liquid separation tank, and automatically control the Liquid level adjusting valve to adjust
State the working condition of condensate pump.
6. pressure-controlled steam exhaust recovering device according to claim 4, it is characterised in that：The top of the fluid-tight plate is away from described
The height of vapor-liquid separation pot bottom is 200~500 mm.
7. pressure-controlled steam exhaust recovering device according to claim 2, it is characterised in that：The steam exhaust circulating cooling component packet
It includes air cooler, de- vapour tank, the steam exhaust line of return and diversion pipe, the air cooler to be arranged above the vapor-liquid separation tank, and logical
It crosses vapour phase pipeline to be connected to the vapor-liquid separation tank, the de- vapour tank is connected to the other end of the air cooler, and the steam exhaust is returned
Loop line is arranged in the top of the air cooler and the de- vapour tank, the both ends of the steam exhaust line of return respectively with the air cooler with
And the de- vapour tank connection, the upper end of the diversion pipe are connected to the bottom of the de- vapour tank, the lower end of the diversion pipe and institute
State connection inside vapor-liquid separation tank.
8. pressure-controlled steam exhaust recovering device according to claim 7, it is characterised in that：The diversion pipe is in vertical direction
30 ° of predetermined angle.
9. pressure-controlled steam exhaust recovering device according to claim 7, it is characterised in that：The frequency conversion voltage controlled component includes pressure
Force snesor, frequency-variable controller and motor, the motor are connect with the fan of the air cooler, the pressure sensor
Pressure for detecting the vapor-liquid separation tank inner tip, the frequency-variable controller is according to the testing number of the pressure sensor
According to the operation power for controlling the motor, to accordingly adjust the live load of the air cooler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820560828.6U CN208059606U (en) | 2018-04-19 | 2018-04-19 | A kind of pressure-controlled steam exhaust recovering device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820560828.6U CN208059606U (en) | 2018-04-19 | 2018-04-19 | A kind of pressure-controlled steam exhaust recovering device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208059606U true CN208059606U (en) | 2018-11-06 |
Family
ID=63983265
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820560828.6U Withdrawn - After Issue CN208059606U (en) | 2018-04-19 | 2018-04-19 | A kind of pressure-controlled steam exhaust recovering device |
Country Status (1)
| Country | Link |
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| CN (1) | CN208059606U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108458599A (en) * | 2018-04-19 | 2018-08-28 | 武汉轻工大学 | A kind of pressure-controlled steam exhaust recovering device and method |
| CN112503965A (en) * | 2020-12-03 | 2021-03-16 | 江苏润云纺织科技有限公司 | Condensate water recovery unit for textile production equipment |
-
2018
- 2018-04-19 CN CN201820560828.6U patent/CN208059606U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108458599A (en) * | 2018-04-19 | 2018-08-28 | 武汉轻工大学 | A kind of pressure-controlled steam exhaust recovering device and method |
| CN108458599B (en) * | 2018-04-19 | 2024-05-07 | 武汉轻工大学 | Pressure-controlled exhaust steam recovery device and method |
| CN112503965A (en) * | 2020-12-03 | 2021-03-16 | 江苏润云纺织科技有限公司 | Condensate water recovery unit for textile production equipment |
| CN112503965B (en) * | 2020-12-03 | 2023-05-23 | 江苏润云纺织科技有限公司 | Condensate water recovery unit for textile production equipment |
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