CN205187982U - Uasb reactor - Google Patents
Uasb reactor Download PDFInfo
- Publication number
- CN205187982U CN205187982U CN201520926201.4U CN201520926201U CN205187982U CN 205187982 U CN205187982 U CN 205187982U CN 201520926201 U CN201520926201 U CN 201520926201U CN 205187982 U CN205187982 U CN 205187982U
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- CN
- China
- Prior art keywords
- reactor body
- phase separation
- reactor according
- uasb
- uasb reactor
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000005191 phase separation Methods 0.000 claims abstract description 19
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 239000010802 sludge Substances 0.000 claims description 14
- 230000009189 diving Effects 0.000 claims description 8
- 230000000630 rising effect Effects 0.000 claims description 5
- 239000010865 sewage Substances 0.000 abstract description 12
- 238000005516 engineering process Methods 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
UASB reactor. Relates to the field of sewage treatment technology. Three -phase separation is effectual, the treatment effeciency is high. Including reactor noumenon and the system of intaking, the inside from the bottom up of reactor noumenon is equipped with reaction zone and three -phase separation district in proper order, be equipped with the mud bed in the reaction zone, be equipped with the three -phase separation ware in the three -phase separation district, the system of intaking is including locating the impulse generator on reactor noumenon upper portion, locate the inside standpipe of reactor noumenon with locate the distributing water pipe of reactor noumenon bottom, the last inlet tube that is equipped with of impulse generator. The utility model discloses three -phase separation is effectual, high treatment efficiency.
Description
Technical field
The utility model relates to technical field of sewage, particularly relates to a kind of UASB reactor.
Background technology
UASB reactor, mainly sewage first after anaerobic reaction, organic substance decomposing in sewage is become gas, then realizing solid, liquid, gas three phase separation, is equipment conventional in sewage disposal, but in now common anaerobic reaction tower, gas-liquid separation is incomplete, a lot of moisture can enter in collection chamber, and scum silica frost also can be attached on bubble enters in collection chamber, finally causes three phase separation weak effect.Separately, when processing sewage of low concentration at normal temperatures, because gas production rate is few, be easy in Sludge Bed form short stream and dead band, make processing efficiency decline or reactor be difficult to normal operation.
Utility model content
The utility model, for above problem, provides the UASB reactor that a kind of three phase separation is effective, processing efficiency is high.
The technical solution of the utility model is: comprise reactor body and water inlet system, and described reactor body inside is provided with reaction zone and three-phase separation area from top to bottom successively, is provided with Sludge Bed in described reaction zone, is provided with triphase separator in described three-phase separation area;
The water distributing pipe that described water inlet system comprises the surge generator being located at described reactor body top, the vertical tube being located at described reactor body inside and is located at bottom described reactor body, described surge generator is provided with water inlet pipe.
Also comprise diving mixer, described diving mixer to be positioned at above water distributing pipe and to be positioned at below Sludge Bed.
Be provided with separate chamber and collection chamber in described triphase separator, the top of described separate chamber comprises back up pad and cross section is the gas skirt of inverted-V-shaped, and the bottom of described collection chamber is provided with reflector, and the top of described collection chamber is provided with vapor pipe.
The top of described triphase separator is provided with effluent weir, and the side of described effluent weir is provided with water leg, on described reactor body, is provided with rising pipe by described water leg.
The top of described triphase separator is provided with settling region, and the top of described settling region is provided with skimming plate.
Described skimming plate is downward-sloping spirrillum.
The bottom of described reactor body is provided with slag-drip opening.
Described reactor body is provided with manhole and some thief holes.
The triphase separator of some even circumferentials arrangement is provided with in described three-phase separation area.
Angle bottom described water distributing pipe and described reactor body is 30 ~ 45 °.
The beneficial effects of the utility model are: 1) three phase separation is effective: establish separate chamber and collection chamber in triphase separator, sewage is after separate chamber's three phase separation, gas is discharged through venting port after entering collection chamber, water overflows through effluent weir after skimming plate pushing off the slag, and solid is then settled down to reactor bottom by self gravitation effect; 2) processing efficiency is high: be provided with diving mixer in the mud section of reactor, regularly stir mud, in case the heavy collection of mud, sewage is fully contacted with Sludge Bed, fast reaction speed, improves processing efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment,
Fig. 2 is the water distributing pipe structural representation of the utility model embodiment;
In figure, 1 is surge generator, and 2 is vertical tubes, and 3 is water distributing pipes, 4 is diving mixers, and 5 is separate chambers, and 501 is back up pads, 502 is gas skirts, and 601 is collection chambers one, and 602 is collection chambers two, 701 is vapor pipes one, and 702 is vapor pipes two, and 8 is effluent weirs, 801 is water legs, and 802 is rising pipes, and 9 is skimming plates, 10 is slag-drip openings, and 11 is manholes.
Embodiment
Below in conjunction with accompanying drawing, the utility model is illustrated.
Fig. 1 is an embodiment of the present utility model, comprise reactor body and water inlet system, described reactor body inside is provided with reaction zone and three-phase separation area from top to bottom successively, is provided with Sludge Bed in described reaction zone, is provided with triphase separator in described three-phase separation area;
The arrangement that described water inlet system comprises the surge generator 1 being located at described reactor body top, the vertical tube 2 being located at described reactor body inside and is located at the water distributing pipe 3(water distributing pipe 3 bottom described reactor body as shown in Figure 2), described water distributing pipe 3 is 30 ~ 45 ° with the angle bottom described reactor body, increase the collision of water and reactor body, strengthen flow velocity; Described surge generator 1 is provided with water inlet pipe 101.
Also comprise diving mixer 4, described diving mixer 4 to be positioned at above water distributing pipe 3 and to be positioned at below Sludge Bed.
Separate chamber 5 and collection chamber (in Fig. 1 collection chamber 1 and collection chamber 2 602) is provided with in described triphase separator, the top of described separate chamber 5 comprises the gas skirt 502 that back up pad 501 and cross section are inverted-V-shaped, the bottom of described collection chamber is provided with reflector, and the top of described collection chamber is provided with vapor pipe (in Fig. 1 vapor pipe 1 and vapor pipe 2 702).
The top of described triphase separator is provided with effluent weir 8, and the side of described effluent weir 8 is provided with water leg 801, on described reactor body, is provided with rising pipe 802 by described water leg 801.
The top of described triphase separator is provided with settling region, and the top of described settling region is provided with skimming plate 9.Described skimming plate 9 is downward-sloping spirrillum.
The bottom of described reactor body is provided with slag-drip opening 10.
Described reactor body is provided with manhole 11 and some thief holes, is convenient to the sewage disposal situation in Real Time Observation reactor.
The triphase separator of some even circumferentials arrangement is provided with in described three-phase separation area.
Principle of work of the present utility model: retain a large amount of anaerobic sludge in reaction zone, bottom, the mud with good sedimentation function and cohesion performance forms sludge blanket in bottom.Sewage to be processed carries out mixing through water distributing pipe 3 water distribution inflow with mud sludge blanket from surge generator 1 and contacts after vertical tube 2, and the organism in the microbial decomposition sewage in mud, is converted into biogas it.Biogas is constantly released with micro-bubble form, micro-bubble is in uphill process, continuous merging, form larger bubble gradually, rise on Sludge Bed top together with water enter triphase separator because the stirring of biogas forms the thinner mud of sludge concentration, when biogas encounters reflector, be folded to the surrounding of reflector, then collection chamber is entered through water layer, then through discharging (available conduit derivation) from venting port, solid-liquid mixed solution enters the settling region of triphase separator through reflection, mud in sewage flocculates, particle increases gradually, and sedimentation under gravity.The mud be settled down on skew wall slides back in reaction zone along skew wall, makes the mud that in reaction zone, accumulation is a large amount of, then discharges Sludge Bed, finally discharge from slag-drip opening 10.Process water outlet after being separated with mud is overflow to water leg 801 from the top of settling region effluent weir 8, then discharges from rising pipe 802.
Claims (10)
1.UASB reactor, comprises reactor body and water inlet system, it is characterized in that, described reactor body inside is provided with reaction zone and three-phase separation area from top to bottom successively, is provided with Sludge Bed in described reaction zone, is provided with triphase separator in described three-phase separation area;
The water distributing pipe that described water inlet system comprises the surge generator being located at described reactor body top, the vertical tube being located at described reactor body inside and is located at bottom described reactor body, described surge generator is provided with water inlet pipe.
2. UASB reactor according to claim 1, is characterized in that, also comprise diving mixer, and described diving mixer to be positioned at above water distributing pipe and to be positioned at below Sludge Bed.
3. UASB reactor according to claim 1, it is characterized in that, separate chamber and collection chamber is provided with in described triphase separator, the top of described separate chamber comprises back up pad and cross section is the gas skirt of inverted-V-shaped, the bottom of described collection chamber is provided with reflector, and the top of described collection chamber is provided with vapor pipe.
4. UASB reactor according to claim 1, is characterized in that, the top of described triphase separator is provided with effluent weir, and the side of described effluent weir is provided with water leg, on described reactor body, is provided with rising pipe by described water leg.
5. UASB reactor according to claim 1, is characterized in that, the top of described triphase separator is provided with settling region, and the top of described settling region is provided with skimming plate.
6. UASB reactor according to claim 5, is characterized in that, described skimming plate is downward-sloping spirrillum.
7. UASB reactor according to claim 1, is characterized in that, the bottom of described reactor body is provided with slag-drip opening.
8. UASB reactor according to claim 1, is characterized in that, described reactor body is provided with manhole and some thief holes.
9. UASB reactor according to claim 1, is characterized in that, is provided with the triphase separator of some even circumferentials arrangement in described three-phase separation area.
10. UASB reactor according to claim 1, is characterized in that, the angle bottom described water distributing pipe and described reactor body is 30 ~ 45 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520926201.4U CN205187982U (en) | 2015-11-19 | 2015-11-19 | Uasb reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520926201.4U CN205187982U (en) | 2015-11-19 | 2015-11-19 | Uasb reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205187982U true CN205187982U (en) | 2016-04-27 |
Family
ID=55780998
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520926201.4U Expired - Fee Related CN205187982U (en) | 2015-11-19 | 2015-11-19 | Uasb reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205187982U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105836880A (en) * | 2016-05-31 | 2016-08-10 | 陕西科技大学 | ASBR (anaerobic sequencing batch reactor) |
-
2015
- 2015-11-19 CN CN201520926201.4U patent/CN205187982U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105836880A (en) * | 2016-05-31 | 2016-08-10 | 陕西科技大学 | ASBR (anaerobic sequencing batch reactor) |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160427 Termination date: 20191119 |