CN103801217B - Evaporative type pipeline system humidifying device - Google Patents
Evaporative type pipeline system humidifying device Download PDFInfo
- Publication number
- CN103801217B CN103801217B CN201410073722.XA CN201410073722A CN103801217B CN 103801217 B CN103801217 B CN 103801217B CN 201410073722 A CN201410073722 A CN 201410073722A CN 103801217 B CN103801217 B CN 103801217B
- Authority
- CN
- China
- Prior art keywords
- blind plate
- cylinder
- end socket
- water inlet
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000003595 mist Substances 0.000 claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 239000012530 fluid Substances 0.000 claims description 15
- 238000003466 welding Methods 0.000 claims description 11
- 238000013016 damping Methods 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- 210000003141 lower extremity Anatomy 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 8
- 229920006395 saturated elastomer Polymers 0.000 abstract description 6
- 230000006641 stabilisation Effects 0.000 abstract 1
- 238000011105 stabilization Methods 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
Abstract
The invention relates to an evaporative type pipeline system humidifying device. The device comprises a cylinder body, a dry-gas inlet pipeline, a wet-gas outlet pipeline, a mist catcher, a blind plate, a water inlet pipe, a plug, a heating pipe and a liquid level control valve, wherein one end of the cylinder body is sealed by the plug and the other end of the cylinder body is sealed by the blind plate; the upper part in the cylinder body is provided with the mist catcher; the top part of the cylinder body is provided with the dry-gas inlet pipeline and the wet-gas outlet pipeline; the water inlet pipe and the liquid level control valve are arranged on the blind plate; the drain pipe is arranged at the bottom of the cylinder body; a flange is arranged on the plug; one end of the heating pipe is provided with a joint and the other of the heating pipe is deeply inserted into the cylinder body; the joint is fixedly connected with the flange. Wet steam is generated in an evaporative manner, and large contact space and long contact time between the inlet gas and the wet steam can be realized, so that the gas is humidified completely to reach a saturation state; the continuous humidifying to the gas with a certain pressure can be realized under the pipeline running condition, the stable running of the pipeline is guaranteed, the liquid drop entrainment is reduced, and the stabilization of the saturated wet gas is guaranteed.
Description
Technical field
The invention belongs to gas humidification technical field in pressure line, in particular it relates to a kind of vaporation-type tubing adds
Wet device.
Background technology
In the scientific research of gas dehydration and humid air dehumidifying, it usually needs carry out gas and reach saturated with moisture state, so
Carry out the experimentation work of correlation afterwards according to experiment purpose.But generally, it is typically up to from compressor outlet effluent air
Less than the saturation of gas, by other means are needed the air-flow of compressor outlet to be humidified so as to be reached saturation shape
State.Particularly in dehydration experiment, because the pressure of pipeline system is higher, in the urgent need to develop with pressure under the conditions of pipeline add
Wet system.
Patent zl01814052.1 proposes a kind of evaporative humidifier producing steam by evaporation, and this device is at a bottom
On seat, a water pot is installed to be used for accommodating a certain amount of water and blower chamber, middle, a columnar wick filtration is installed
Then the steam of evaporation flowed through wick cylinder side wall and discharge from air vent by device.Patent zl200610065844.x proposes one
Kind of ultrasonic type air humidifier, this device made using ultrasonic transducer the water in storage tank occur vibrations with machine box opening
Produce steam in the vertical tube of connection, and be provided with air vent on machine box opening, ultrasonic generation steam is finally discharged from air vent.
Above-mentioned vaporation-type and ultrasonic type humidifier are all only applicable to airspace is humidified it is impossible to be realized to pressure
Pipe-line equipment system humidified.
Content of the invention
For the defect overcoming prior art to exist, for the requirement of pressure line gas humidification, the present invention provides a kind of steaming
Hairdo tubing damping device, this device enables to complete the humidification to pipeline gas under the conditions of certain pressure, makes gas
Saturation can be reached.
For achieving the above object, the technical solution used in the present invention is as follows:
Vaporation-type tubing damping device, comprising: cylinder, dry gas suction line, damp exit pipeline, mist eliminator, blind
Plate, water inlet pipe, end socket, heating tube, fluid level control valve；One end of cylinder is closed by end socket, the other end is closed by blind plate, cylinder,
End socket, blind plate form airtight humidification system；Top in cylinder is provided with mist eliminator, and the top of cylinder is provided with dry gas entrance
Pipeline, damp exit pipeline；On blind plate, water inlet pipe and fluid level control valve are installed, drain pipe is arranged on the bottom of cylinder, on end socket
Flange is installed, heating tube one end is provided with joint, the other end gos deep in cylinder, and joint is fixedly connected with flange.
With respect to prior art, the present invention has a following beneficial effect:
1st, the present invention adopts evaporation mode to produce damp steam, and tank endogenous dampness vapor space is larger, can make gas and damp steam
There are larger attaching space and longer time of contact, gas is fully humidified, make gas reach saturation；
2nd, assembly of the invention is a kind of airtight humidification system, it is possible to achieve to certain pressure under the conditions of pipeline performance
Gas is continuously humidified, and ensures the stable operation of pipeline；
3rd, the present invention adopts mist eliminator to design, and multilamellar stainless steel filter screen can reduce in gas-liquid mixing process effectively
Liquid splash, reduces gas to carrying secretly of drop it is ensured that stablizing of saturated with moisture.
Brief description
Fig. 1 is the structural representation of vaporation-type tubing damping device；
Fig. 2 is water inlet pipe, fluid level control valve and blind plate scheme of installation；
Fig. 3 is end socket and flange scheme of installation；
In figure: 1, cylinder, 2, dry gas suction line, 3, mist eliminator, 4, damp exit pipeline, 5, water inlet pipe, 6, liquid level control
Valve processed, 7, blind plate, 8, drain pipe, 9, heating tube, 10, support, 11, flange, 12, joint, 13, end socket.
Specific embodiment
As shown in Figure 1, Figure 2, Figure 3 shows, vaporation-type tubing damping device, comprising: cylinder 1, dry gas suction line 2, wet
Gas outlet line 4, mist eliminator 3, blind plate 7, water inlet pipe 5, end socket 13, heating tube 9, fluid level control valve 6.
Cylinder 1 is rustless steel cylindrical shell, and cylinder 1 supports by support 10, and one end of cylinder 1 closed by end socket 13, another
End is closed by blind plate 7, and blind plate 7 is fixedly connected with cylinder 1 by welding manner with end socket 13, and cylinder 1, end socket, blind plate form close
The humidification system closing, it is possible to achieve under the conditions of pipeline performance, certain pressure gas is continuously humidified, ensures the company of pipeline
Continuous stable operation.
A diameter of 1200mm～5000mm of cylinder 1, length is 2000mm～8000mm, and wall thickness is 4mm～26mm；End socket
13 a diameter of 1200mm～5000mm, thickness is 20mm～130mm；A diameter of 1200mm～5000mm of blind plate 7, thickness is
20mm～130mm.
Top in cylinder 1 is provided with mist eliminator 3, and mist eliminator 3 adopts 2～4 layers of stainless steel filter screen, and mesh size is
50～300 mesh, mist eliminator 3 is horizontally disposed with, and is fixedly connected with end socket 13, blind plate 7 by welding manner, cylinder 1 inside top surface with
Mist eliminator 3 is at a distance of 45-500mm；Using mist eliminator design, multilamellar stainless steel filter screen can reduce gas-liquid mixing process effectively
In liquid splash, reduce gas to carrying secretly of drop it is ensured that stablizing of saturated with moisture.
The top of cylinder 1 is provided with dry gas suction line 2, damp exit pipeline 4；The centre distance of dry gas suction line 2
End socket 200mm～500mm, damp exit pipeline 4 centre distance blind plate 200mm～500mm；Dry gas suction line 2, damp exit
Pipeline 4 is fixedly connected with cylinder 1 by welding manner.
Dry gas suction line 2 is stainless pipe, a diameter of 25mm～150mm, and wall thickness is 1mm～2.8mm, dry gas entrance
Pipeline 2 outlet is located at mist eliminator 3 lower section 30mm～120mm；Damp exit pipeline 4 is stainless pipe, a diameter of 25mm～
150mm, wall thickness is 1mm～2.8mm.
Water inlet pipe 5 and fluid level control valve 6 installed on blind plate 7, water inlet pipe 5 and fluid level control valve 6 pass through welding manner and blind
Plate 7 is fixedly connected；The center of fluid level control valve 6 and blind plate 7 center superposition, water inlet pipe 5 is located on the center of blind plate 7, water inlet
The centre distance blind plate 7 center 80mm～220mm (water inlet pipe 5 and blind plate 7 are centrally located in same plumb line) of pipe 5；Water inlet
A diameter of 15mm～50mm of pipe 10, wall thickness is 1mm～2.8mm, a diameter of 10mm～50mm of fluid level control valve 6, and wall thickness is
1mm～1.8mm.
Drain pipe 8 is arranged on the bottom of cylinder 1, using stainless pipe, a diameter of 10mm～50mm of drain pipe 8, wall
Thick is 1mm～4.5mm, and drain pipe 8 center is 80mm～200mm with the distance of blind plate 7；Drain pipe 8 passes through welding manner and cylinder
Body 1 is fixedly connected.
The number of support 10 is 2, is 200mm～2000mm near the support of end socket and the distance of end socket 13；Near blind
The support of plate is 200mm～2000mm with the distance of blind plate 7.
Flange 11, flange 11 centre distance end socket 13 lower limb 120mm～500mm, flange 11 He are provided with end socket 13
End socket 13 is fixedly connected by welding manner；Heating tube 9 one end is provided with joint 12, the other end gos deep in cylinder 1, and joint 12 leads to
Cross bolt to be fixedly connected with flange 11；The length of heating tube 9 is 200～500mm, and power is 3kw～25kw；Flange 11 is straight
Footpath is 80mm～500mm, and wall thickness is 1mm～2.8mm；A diameter of 80mm～500mm of joint 12, thickness is 20mm～130mm.
Damp steam is produced using evaporation mode, is conducive to increasing the contact area of dry gas and moist steam, gas is fully humidified；And
And tank endogenous dampness vapor space is larger, can make gas and damp steam to have longer attaching space and time, make gas reach saturation
State.
The specific workflow of the present invention is: aqueous water enters cylinder 1 by water inlet pipe 5, and water level is controlled by fluid level control valve 6
System, water closes water inlet pipe 5 and fluid level control valve 6 after adding well；Open heating tube 9 and aqueous water is carried out with humidification evaporation, produce wet steaming
Gas, unsaturated gas enters cylinder 1 by dry gas suction line 2, so that unsaturated gas is produced with damp steam and sufficiently contacts, to gas
Body is humidified；Drop in saturated with moisture is filtered out by mist eliminator；Finally, through filtration saturated with moisture from damp exit
Pipeline 4 flows out.
Claims (1)
1. a kind of vaporation-type tubing damping device, comprising: cylinder, dry gas suction line, damp exit pipeline, mist eliminator,
Blind plate, water inlet pipe, end socket, heating tube, fluid level control valve；It is characterized in that: one end of cylinder is closed by end socket, the other end is by blind
Plate is closed, and cylinder, end socket, blind plate form airtight humidification system；Top in cylinder is provided with mist eliminator, the top peace of cylinder
Equipped with dry gas suction line, damp exit pipeline；Water inlet pipe and fluid level control valve are installed on blind plate, drain pipe is arranged on cylinder
Bottom, end socket is provided with flange, and heating tube one end is provided with joint, the other end gos deep in cylinder, and joint is fixing with flange even
Connect, cylinder is supported by support, mist eliminator adopts 2～4 layers of stainless steel filter screen, mist eliminator is horizontally disposed with, mist eliminator passes through weldering
The mode that connects is fixedly connected with end socket, blind plate；Dry gas suction line, damp exit pipeline pass through welding manner and cylinder is fixing even
Connect, the outlet of dry gas suction line is located at 30mm～120mm below mist eliminator, water inlet pipe and fluid level control valve pass through welding manner and
Blind plate is fixedly connected；The center of fluid level control valve and blind plate center superposition, water inlet pipe is located on the center of blind plate, flange center
Apart from end socket lower limb 120mm～500mm, flange is fixedly connected by welding manner with end socket；Joint passes through bolt and flange
It is fixedly connected；The number of support is 2, and water inlet pipe and blind plate are centrally located in same plumb line；
Blind plate is fixedly connected with cylinder by welding manner with end socket, and cylinder is rustless steel cylindrical shell；
Inner barrel top surface and mist eliminator are at a distance of 45-500mm；
A diameter of 1200mm～5000mm of cylinder, length is 2000mm～8000mm, and wall thickness is 4mm～26mm；End socket straight
Footpath is 1200mm～5000mm, and thickness is 20mm～130mm；A diameter of 1200mm～5000mm of blind plate, thickness be 20mm～
130mm；
The centre distance end socket 200mm～500mm of dry gas suction line, damp exit pipe center apart from blind plate 200mm～
500mm；
Dry gas suction line is stainless pipe, and damp exit pipeline is stainless pipe；
The centre distance blind plate center 80mm～220mm of water inlet pipe；A diameter of 15mm～50mm of water inlet pipe, wall thickness be 1mm～
2.8mm, a diameter of 10mm～50mm of fluid level control valve, wall thickness is 1mm～1.8mm；
Drain pipe adopts stainless pipe, a diameter of 10mm～50mm of drain pipe, and wall thickness is 1mm～4.5mm, draining tube hub
Distance with blind plate is 80mm～200mm；Drain pipe is fixedly connected with cylinder by welding manner；
The length of heating tube is 200～500mm, and power is 3kw～25kw；Flange diameter is 80mm～500mm, and wall thickness is 1mm
～2.8mm；A diameter of 80mm～500mm of joint, thickness is 20mm～130mm；
It is 200mm～2000mm near the support of end socket and the distance of end socket；Near the support of blind plate with the distance of blind plate it is
200mm～2000mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410073722.XA CN103801217B (en) | 2014-02-28 | 2014-02-28 | Evaporative type pipeline system humidifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410073722.XA CN103801217B (en) | 2014-02-28 | 2014-02-28 | Evaporative type pipeline system humidifying device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103801217A CN103801217A (en) | 2014-05-21 |
| CN103801217B true CN103801217B (en) | 2017-01-25 |
Family
ID=50698892
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410073722.XA Expired - Fee Related CN103801217B (en) | 2014-02-28 | 2014-02-28 | Evaporative type pipeline system humidifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103801217B (en) |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102005001992B4 (en) * | 2005-01-15 | 2012-08-02 | Palas Gmbh Partikel- Und Lasermesstechnik | Method and device for counting particles |
| CN201162028Y (en) * | 2007-11-30 | 2008-12-10 | 中冶南方工程技术有限公司 | Fore-warmer tank |
| CN101195777B (en) * | 2007-12-04 | 2013-02-13 | 沈阳荣林科技发展有限公司 | Natural gas humidification steam generation mixer |
| CN101832182A (en) * | 2009-03-11 | 2010-09-15 | 中国科学院工程热物理研究所 | Synthesis gas humidifier and heating and humidifying method |
| CN203725095U (en) * | 2014-02-28 | 2014-07-23 | 常州大学 | Evaporative typehumidifying device for pipeline system |
-
2014
- 2014-02-28 CN CN201410073722.XA patent/CN103801217B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN103801217A (en) | 2014-05-21 |
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| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170125 |
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