CN208839275U - A kind of methane recovery steam-water separator - Google Patents
A kind of methane recovery steam-water separator Download PDFInfo
- Publication number
- CN208839275U CN208839275U CN201821351193.5U CN201821351193U CN208839275U CN 208839275 U CN208839275 U CN 208839275U CN 201821351193 U CN201821351193 U CN 201821351193U CN 208839275 U CN208839275 U CN 208839275U
- Authority
- CN
- China
- Prior art keywords
- spin chamber
- net layer
- metal net
- baffling
- baffling room
- 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
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 238000011084 recovery Methods 0.000 title claims abstract description 13
- 229910052751 metal Inorganic materials 0.000 claims abstract description 29
- 239000002184 metal Substances 0.000 claims abstract description 29
- 238000005192 partition Methods 0.000 claims abstract description 8
- 238000004891 communication Methods 0.000 claims abstract description 4
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 3
- 239000000956 alloy Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 238000000855 fermentation Methods 0.000 description 4
- 230000000903 blocking effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses a kind of methane recovery steam-water separators, including spin chamber, baffling room, metal net layer, the spin chamber, baffling room, metal net layer be sequentially connected with integrally change it is columnar structured, the spin chamber axle center is horizontally disposed rotary shaft, helical blade is evenly arranged in the rotary shaft, the rotary shaft is connected with the motor being arranged on the outside of the spin chamber, spin chamber's end sides are provided with air inlet, the spin chamber bottom is provided with the first discharge outlet, partition is provided between the spin chamber and baffling room, communication port is provided on the partition, baffle plate is distributed in space crossings on the baffling indoor, baffling room bottom is provided with the second discharge outlet, the metal net layer is provided with equally distributed metal mesh, and the end of the metal net layer is provided with gas outlet, pass through three sections Steam-water separation substantially increases water removal effect.
Description
Technical field
The utility model belongs to methane recovery equipment technical field, and in particular to a kind of methane recovery steam-water separator.
Background technique
With the appearance of China's Renewable Energy Law, people start to carry out each intermediate item skill of renewable energy to greatest extent
The research and development of art, anaerobic fermentation technology are to generate biogas by fermenting to biomass castoffs such as farming and animal husbandries and carry out
A kind of technology of power generation, has been widely used.Therefore, in order to improve the efficiency and stability of anaerobic fermentation system,
People in anaerobic fermentation process all kinds of devices and Processing Technology Research it is more and more.Anaerobic fermentation process temperature is relatively
Height contains moisture in biogas, while can be right if containing large quantity of moisture in biogas containing sulfurous gas such as hydrogen sulfide in biogas
Conveyance conduit has corrosion, so, the processing of water is just particularly important in biogas.Moisture is easy in the water removal device of the prior art
Evaporation takes away the water being collected by biogas again, therefore removes water inefficient.
Utility model content
The utility model solves the deficiencies in the prior art, provide it is a kind of including spin chamber, baffling room, metal net layer natural pond
Gas recycling substantially increases water removal effect by three sections of steam-water separations with steam-water separator, and the service life used is long.
The technical scheme adopted by the utility model is a kind of methane recovery steam-water separator, including spin chamber, baffling
Room, metal net layer, the spin chamber, baffling room, metal net layer, which are sequentially connected with, integrally changes columnar structured, spin chamber's axis
The heart is horizontally disposed rotary shaft, helical blade is evenly arranged in the rotary shaft, the rotary shaft and setting are in institute
It states motor on the outside of spin chamber to be connected, spin chamber's end sides are provided with air inlet, and the spin chamber bottom is provided with the
One discharge outlet is provided with partition between the spin chamber and baffling room, be provided with communication port on the partition, in the baffling room
Intersect on side and be intervally distributed with baffle plate, baffling room bottom is provided with the second discharge outlet, and the metal net layer is provided with
The metal mesh of even distribution, and the end of the metal net layer is provided with gas outlet.
Preferably, the spin chamber bottom is provided with oblique flow plate.
It is furthermore preferred that the baffle plate is bow-shaped structural.
Even more preferably, first discharge outlet and the second discharge outlet end are mounted on filter.
Even more preferably, the spin chamber, baffling room and metal net layer are all made of titanium alloy material and are made.
Compared to the prior art, the utility model has the advantages that a kind of methane recovery steam-water separator, including
Spin chamber, baffling room, metal net layer, when biogas passes through spin chamber, the blocking air-flow by helical blade will be become by linear motion
For circular motion, marsh gas flow generates centrifugal force during rotation, and the biggish drop of density is got rid of to spin chamber's barrel, liquid
Drop just loses inertia force and momentum and downward gravity by entrance velocity are along spin chamber's barrel once contact with spin chamber's barrel
It falls, hence into the first discharge outlet；When biogas passes through baffling room, change when encountering baffle plate flow direction, dry biogas can be with
Continue forward around baffle plate, and water droplet can accumulate on baffle plate, finally fall on the bottom of baffling room；Biogas passes through metal mesh
Layer when, the water droplet of suspension is adsorbed after encountering metal mesh, water droplet greatly to a certain extent after, due to gravity fall.
Detailed description of the invention
Fig. 1 is the utility model structure diagram.
Specific embodiment
The utility model is described in detail with reference to the accompanying drawings and detailed description.
A kind of methane recovery steam-water separator, refering to fig. 1, including spin chamber 1, baffling room 2, metal net layer 3, the rotation
Flow chamber 1, baffling room 2, metal net layer 3, which are sequentially connected with, integrally to be changed columnar structured, and 1 axle center of spin chamber is set in the horizontal direction
It is equipped with rotary shaft 11, helical blade 12 is evenly arranged in the rotary shaft 11, the rotary shaft 11 is with setting in the eddy flow
The motor 13 in the outside of room 1 is connected, and 1 end sides of spin chamber are provided with air inlet 14, and 1 bottom of spin chamber is provided with the
One discharge outlet 15, when biogas passes through spin chamber 1, the blocking air-flow by helical blade 12 will be become circumference fortune from linear motion
Dynamic, marsh gas flow generates centrifugal force during rotation, the biggish drop of density is got rid of to 1 barrel of spin chamber, drop is once
It is contacted with 1 barrel of spin chamber, just loses inertia force and momentum and downward gravity by admission velocity are under 1 barrel of spin chamber
It falls, hence into the first discharge outlet 15, partition 16 is provided between the spin chamber 1 and baffling room 2, is arranged on the partition 16
There is communication port 17, upper intersection is intervally distributed with baffle plate 21 on the inside of the baffling room 2, and 2 bottom of baffling room is provided with second
Discharge outlet 22 when biogas passes through baffling room 2, changes, dry biogas can bypass baffle plate 21 when encountering 21 flow direction of baffle plate
Continue forward, and water droplet can accumulate on baffle plate 21, finally fall on the bottom of baffling room 2, and the metal net layer 3 is provided with
Equally distributed metal mesh, the end of the metal net layer 3 are provided with gas outlet 31, and the water droplet of suspension encounters quilt after metal mesh
Absorption, water droplet greatly to a certain extent after, due to gravity fall.
With continued reference to Fig. 1,1 bottom of spin chamber is provided with oblique flow plate 18, flows into the first row mouth of a river 15 convenient for liquid.
With continued reference to Fig. 1, the baffle plate 21 is bow-shaped structural, changes the motion path of marsh gas flow.
With continued reference to Fig. 1, first discharge outlet 15 and 22 end of the second discharge outlet are mounted on filter, convenient for filtering
Fall the impurity in liquid.
With continued reference to Fig. 1, the spin chamber 1, baffling room 2 and metal net layer 3 are all made of titanium alloy material and are made, and titanium closes
The corrosion-resistant service life to extend steam-water separator of golden material.
When work, motor 13, blocking gas when biogas passes through spin chamber 1 by air inlet 14, by helical blade 12 are opened
Stream will be become circular motion from linear motion, and marsh gas flow generates centrifugal force during rotation, by the biggish drop of density
Get rid of to 1 barrel of spin chamber, drop is once contacted with 1 barrel of spin chamber, just lose inertia force and by the momentum of admission velocity and to
Under gravity fall along 1 barrel of spin chamber, hence into the first discharge outlet 15, when biogas passes through baffling room 2, when encountering baffle plate
21 flow directions change, and dry biogas can continue forward around baffle plate 21, and water droplet will accumulate on baffle plate 21, finally
Fall on the bottom of baffling room 2, the water droplet of suspension is adsorbed after encountering metal mesh, water droplet greatly to a certain extent after, due to gravity make
With whereabouts, last biogas is discharged by gas outlet 31.
Above-described embodiment, the only preferred embodiment of the utility model not are used to limit the implementation model of the utility model
It encloses, therefore all equivalent variationss done with content described in the utility model claims, the utility model right should all be included in and wanted
Within the scope of asking.
Claims (5)
1. a kind of methane recovery steam-water separator, which is characterized in that including spin chamber (1), baffling room (2), metal net layer
(3), the spin chamber (1), baffling room (2), metal net layer (3), which are sequentially connected with, integrally changes columnar structured, the spin chamber
(1) axle center is horizontally disposed has rotary shaft (11), is evenly arranged with helical blade (12) on the rotary shaft (11), described
Rotary shaft (11) is connected with the motor (13) being arranged on the outside of the spin chamber (1), and spin chamber (1) end sides are provided with
Air inlet (14), spin chamber (1) bottom is provided with the first discharge outlet (15), between the spin chamber (1) and baffling room (2)
It is provided with partition (16), is provided with communication port (17) on the partition (16), intersect on baffling room (2) inside and be spaced apart
Have baffle plate (21), baffling room (2) bottom is provided with the second discharge outlet (22), and the metal net layer (3) is provided with uniformly
The metal mesh of distribution, and the end of the metal net layer (3) is provided with gas outlet (31).
2. a kind of methane recovery steam-water separator as described in claim 1, which is characterized in that spin chamber (1) bottom
It is provided with oblique flow plate (18).
3. a kind of methane recovery steam-water separator as claimed in claim 2, which is characterized in that the baffle plate (21) is bow
Shape structure.
4. a kind of methane recovery steam-water separator as claimed in claim 3, which is characterized in that first discharge outlet (15)
Filter is mounted on the second discharge outlet (22) end.
5. a kind of methane recovery steam-water separator as claimed in claim 4, which is characterized in that the spin chamber (1), baffling
Room (2) and metal net layer (3) are all made of titanium alloy material and are made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821351193.5U CN208839275U (en) | 2018-08-21 | 2018-08-21 | A kind of methane recovery steam-water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821351193.5U CN208839275U (en) | 2018-08-21 | 2018-08-21 | A kind of methane recovery steam-water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208839275U true CN208839275U (en) | 2019-05-10 |
Family
ID=66356041
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821351193.5U Expired - Fee Related CN208839275U (en) | 2018-08-21 | 2018-08-21 | A kind of methane recovery steam-water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208839275U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111203060A (en) * | 2020-01-22 | 2020-05-29 | 王彦军 | Water vapor filtering separator in chemical production |
| CN114515493A (en) * | 2022-04-20 | 2022-05-20 | 河北爱节能源科技有限公司 | High-efficient silicone oil recovery system |
| CN114682007A (en) * | 2022-04-29 | 2022-07-01 | 弗勒锑克(广东)工程设备有限公司 | Steam dry-wet separator |
-
2018
- 2018-08-21 CN CN201821351193.5U patent/CN208839275U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111203060A (en) * | 2020-01-22 | 2020-05-29 | 王彦军 | Water vapor filtering separator in chemical production |
| CN114515493A (en) * | 2022-04-20 | 2022-05-20 | 河北爱节能源科技有限公司 | High-efficient silicone oil recovery system |
| CN114515493B (en) * | 2022-04-20 | 2022-07-19 | 河北爱节能源科技有限公司 | High-efficient silicone oil recovery system |
| CN114682007A (en) * | 2022-04-29 | 2022-07-01 | 弗勒锑克(广东)工程设备有限公司 | Steam dry-wet separator |
| CN114682007B (en) * | 2022-04-29 | 2025-10-24 | 弗勒锑克(广东)工程设备有限公司 | Steam dry-wet separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190510 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |