CN2937099Y - High dispersion spray deammonia tower - Google Patents
High dispersion spray deammonia tower Download PDFInfo
- Publication number
- CN2937099Y CN2937099Y CN 200620097443 CN200620097443U CN2937099Y CN 2937099 Y CN2937099 Y CN 2937099Y CN 200620097443 CN200620097443 CN 200620097443 CN 200620097443 U CN200620097443 U CN 200620097443U CN 2937099 Y CN2937099 Y CN 2937099Y
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- ammonia
- tower
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- remove
- spraying
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Abstract
The utility model provides a high scattering spray ammonia elimination tower without filler and column tray, which comprises a blast blower or an induced drafting fan, a feed water pump, a column of ammonia elimination and an inlet air distributor. The utility model has the advantages of inner high distributing parts inside of ammonia elimination tower, which is positioned at the top of inlet air distributor. The high distributing part comprises an atomizer and a distributing water pipe; the atomizer is arranged upper or lower, connected with feed water pump through distributing water pipe and inlet water pipe. The high distributing parts can treat the nitrogenous effluent highly efficiently due to increasing liquid surface scale; the escape speed of free ammonia from solution is highly increased, so that the utility model can operate reliably with high efficiency of removal of free ammonia and nitrogen from solution and lower power consumption.
Description
Technical field
The utility model relates to the separating device that a kind of dispersion method is removed ammonia nitrogen in the solution.The utility model can be widely used in the processing of the ammonia nitrogen waste water of industries such as petrochemical complex, chemical fertilizer, weaving, agricultural chemicals, biological products as a kind of separating unit of economical and efficient, also can be used for the treating processes of municipal wastewater and percolate.
Background technology
Traditional ammonia nitrogen sewage treatment equipment normally selects air or water vapor to recommend matter as gas, adopts packing tower or tray column that the gas-to-liquid contact interface is provided, to reach the purpose that ammonia is removed from solution.
Adopt the packing tower separating device of air stripping method (being that air gas is carried), though can reach the requirement of part removal of ammonia and nitrogen, it is low to remove efficient, and need the waste water temperature raising winter, otherwise efficient is lower; Because blow-off method operation gas/water is than big (being generally 3000～4000), the ammonia-containing exhaust amount that causes the stripping cat head to be got rid of is big, is unfavorable for the absorption of ammonia, usually directly to airborne release, causes secondary pollution in addition; Blast height (500～800mm H2O) causes the energy consumption height, one ton of waste water power consumption of average treatment, 6～9kW; And because the restriction of vapor liquid equilibrium, blow-off method can only arrive ammonia nitrogen removal～500mg/l, does not reach emission request.
Adopt the packing tower or the tray column separating device of steam gas formulation (promptly adding thermal distillation), (usually＞10000mg/l), ammonia nitrogen waste water that flow is little is handled, but is needed to consume steam and water coolant to be suitable for the ammonia-nitrogen content height.Under 0.3MPa pressure, adopt steam gas to carry the ammonia nitrogen waste water of 30000mg/l, make～10% ammoniacal liquor, one ton of waste water consumption of every processing steam 390kg, water coolant 20t, if 80 yuan/ton of steam prices, 0.10 yuan of/ton calculating of water coolant price, then priming cost is 33.2 yuan/ton; As making liquefied ammonia, one ton of waste water of every processing also need consume steam 490kg and water coolant 25t again, only makes liquefied ammonia 28kg, obviously makes liquefied ammonia and does not more calculate.
Summary of the invention
The purpose of this utility model provides a kind of high dispersive spraying of not only not had filler but also not had a tower tray and removes the ammonia tower, this tower adopts the high dispersive element that ammonia nitrogen waste water is carried out high dispersing and handles, increase considerably the flowing fluid ratio surface-area, greatly improved and be dissolved in the speed that the free ammonia in the water is escaped from liquid phase, with reach ammonia nitrogen removal frank height in the solution, energy consumption is low, the purpose that equipment is reliable.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of high dispersive spraying removes the ammonia tower, comprise gas blower or induced draft fan, service pump, remove ammonia Tata body and air intake sparger, it is characterized in that the high dispersive arrangements of elements is in removing ammonia Tata body, be positioned at the top of air intake sparger, the high dispersive element is by atomizing nozzle and divide water distributor to form, atomizing nozzle is provided with up or down, communicates with service pump by minute water distributor and water inlet pipe.
Above-mentioned high dispersive spraying removes the ammonia tower, it is characterized in that removing in the ammonia Tata body mist eliminator is set, and the high dispersive element is positioned at the top of air intake sparger and the below of mist eliminator.
Above-mentioned high dispersive spraying removes the ammonia tower, it is characterized in that according to former water and clearance requirement, remove in the ammonia tower same, but high dispersive element individual layer or double-deck the layout.
Above-mentioned high dispersive spraying removes the ammonia tower, it is characterized in that the atomizing nozzle of high dispersive element links to each other with a minute water distributor by taking over, and every branch water distributor is arranged several atomizing nozzles.
Above-mentioned high dispersive spraying removes the ammonia tower, it is characterized in that adopting single-stage or multistage setting, or arranges with the subsequent disposal tower and except that ammonia Tata body superposes.Form the arrangement form of the single tower of single-stage or multistage single tower, but the multitower serial or parallel connection uses as required.
The spraying of above-mentioned high dispersive removes the ammonia tower, it is characterized in that described to remove ammonia Tata body be vertical, or adopts horizontal according to field condition; When being horizontal, the high dispersive element is positioned at the rear of air intake sparger, and the atomizing nozzle of high dispersive element is laterally placed.
The spraying of above-mentioned high dispersive removes the ammonia tower, it is characterized in that described to remove ammonia Tata body be steel construction piece, or concrete structure.
Advantage of the present utility model is that the solution that adopts the high dispersive element will contain ammonia nitrogen carries out high dispersing, make it to become small liquid particle, free ammonia shifts to gas phase in the liquid phase speed and probability have been quickened greatly, only need the air of relatively small amount just the ammonia of overflowing can be taken away, its ammonia nitrogen removal mechanism is that liquid height disperses and then generation surface chemistry effect, break blow-off method and removed the restriction that efficient is influenced by the gas-liquid dissolution equilibrium constant, the ammonia nitrogen removal frank height adopts multiple-stage treatment can reach discharging standards; Blow-off method ammonia nitrogen removal principle is based on the vapor liquid equilibrium of solution, therefore must increase gas/water ratio and promptly strengthen the stripping air capacity reduces ammonia to increase inert gas content in the gas phase equilibrium partial pressure, improves the rate of transform of free ammonia.
As add the solution that suitable interpolation auxiliary agent will help to contain ammonia nitrogen and carry out high dispersing, make it to become small liquid particle.
Another remarkable advantage of the present utility model also is its employing void tower spraying, whole tower resistance is little, thereby required air pressure is low, add that this tower operation gas/water is than low, it only is 1/3～1/2 of blow-off method, therefore handle only power consumption 2～2.5kW of one ton of waste water (qualified discharge), reduced energy consumption and processing cost.In addition, this tower has been cancelled filler owing to adopt the void tower operation, avoided because filler corrosion or aging channel and the dead band that produces, and iron rust or fragment is to the obstruction of pipeline, so does not need frequent maintenance, has the advantage of stable and reliable operation.
Description of drawings
Accompanying drawing 2 is the utility model embodiment 2; The downward one deck of nozzle is arranged.
Accompanying drawing 3 is the utility model embodiment 3; Nozzle is two layers of layout upwards.
Accompanying drawing 4 is the utility model embodiment 4; The downward two layers of layout of nozzle.
Accompanying drawing 5 is the utility model embodiment 5; Secondary removes ammonia and arranges.
Accompanying drawing 6 is the utility model embodiment 6; Secondary removes ammonia layout+absorption.
Accompanying drawing 7 is the utility model embodiment 7; Secondary removes ammonia layout+discharging.
Accompanying drawing 8 is the utility model embodiment 8; Induced draft fan.
Accompanying drawing 9 is the utility model embodiment 9; Horizontal layout 1.
Accompanying drawing 10 is the utility model embodiment 10; Horizontal layout 2.
Accompanying drawing 11 is the utility model embodiment high dispersive component structure 1 synoptic diagram.
Among the figure, blower fan 1, air intake sparger 2, high dispersive element 3 removes ammonia Tata body 4, mist eliminator 5, riser 6, absorption tower tower body 7 absorbs shower nozzle 8, emptying cylindrical shell 9, induced draft fan 10,11 bracing members divide water distributor 12,13 water inlet pipes, atomizing nozzle 14.
Embodiment
Below in conjunction with accompanying drawing the utility model embodiment is further described.
In waste water ammonia-nitrogen content not high (＜200mg/l) and the less (3～5m of flow
3/ h) occasion, can adopt the high dispersive spraying as the single-stage individual layer nozzle placement of accompanying drawing 1 to remove ammonia: this tower comprises blower fan 1, air intake sparger 2, high dispersive element 3 removes ammonia Tata body 4 and mist eliminator 5.
Waste water is taken over through water inlet and is entered high dispersive element 3, and under 0.3～0.6MPa pressure, through atomizing nozzle 14 ejections, the nozzle direction both can arrange upwards that (accompanying drawing 1) also can arrange (accompanying drawing 2) downwards by minute water distributor 12; Air improves blast through blower fan 1, goes into tower from removing ammonia tower bottom air intlet pipe, is uniformly distributed in Ta Nei and upwards mobile through air intake sparger 2, and the gas ammonia that will overflow from small solution droplets is taken away rapidly.Cat head is provided with mist eliminator 5, and tower is outer to be established for the minimizing drop is taken out of.
Divide water distributor can be arranged as any suitable manner such as dendroid, ring-type.Removing ammonia Tata body 4 can be round shape or other any suitable cylindricality.
With embodiment 1, in waste water ammonia-nitrogen content not high (＜200mg/l) and the less (3～5m of flow
3/ h) occasion, as select for use the tower body diameter less remove the ammonia tower, then can adopt the high dispersive spraying as the double-deck nozzle placement of single-stage of accompanying drawing 3 to remove ammonia: this tower comprises blower fan 1, air intake sparger 2, high dispersive element 3 removes ammonia Tata body 4 and mist eliminator 5.
Embodiment 5 (referring to accompanying drawing 5 and accompanying drawing 11)
Ammonia-nitrogen content higher (1000～5000mg/l) and the big (＞10m of treatment capacity in waste water
3/ h) occasion, can adopt the high dispersive spraying as the double-deck nozzle placement of twin-stage of accompanying drawing 5 to remove ammonia: this tower comprises blower fan 1, air intake sparger 2, high dispersive element 3 removes ammonia Tata body 4, mist eliminator 5 and riser 6.
Waste water is taken over through water inlet and is entered high dispersive element 3, and under 0.3～0.6MPa pressure, through nozzle 14 ejections, the nozzle direction both can upwards have been arranged also and can have been arranged downwards by minute water distributor 12; Air improves blast through blower fan 1, removes the air intlet pipe of ammonia tower from the bottom and goes into tower, is uniformly distributed in Ta Nei and upwards mobile through air intake sparger 2, and the gas ammonia that will overflow from small solution droplets is taken away rapidly, and removes the ammonia tower after riser 6 enters top.Twin-stage removes the ammonia tower and is particularly suitable for the occasion that ammonia-nitrogen content is higher and wastewater treatment capacity is bigger.The effect of riser 6 is to allow the water flow that contains in the tower of bottom upwards flow, but the water of upper column can not flow down.
Embodiment 6 (referring to accompanying drawing 6 and accompanying drawing 11)
With embodiment 5, ammonia-nitrogen content higher (1000～5000mg/l) and the big (＞10m of treatment capacity in waste water
3/ h) occasion, and the ammonia content in the gas is unsuitable for directly discharging on the spot after secondary removes ammonia, at this moment, can adopt the high dispersive spraying as the double-deck nozzle placement of the twin-stage of accompanying drawing 6 to remove ammonia+ammonia absorber: this tower comprises blower fan 1, air intake sparger 2, high dispersive element 3, remove ammonia Tata body 4, mist eliminator 5, riser 6, absorption tower tower body 7 and absorption shower nozzle 8.
Waste water is taken over through water inlet and is entered high dispersive element 3, and under 0.3～0.6MPa pressure, through nozzle 14 ejections, the nozzle direction both can upwards have been arranged also and can have been arranged downwards by minute water distributor 12; Air improves blast through blower fan 1, removes the air intlet pipe of ammonia tower from the bottom and goes into tower, is uniformly distributed in Ta Nei and upwards mobile through air intake sparger 2, and the gas ammonia that will overflow from small solution droplets is taken away rapidly, and removes the ammonia tower after riser 6 enters the middle part.Air after ammonia is removed at the two poles of the earth enters the absorption tower through riser 6 again, after ammonia nitrogen is removed on the absorption tower, and the direct emptying of tail gas.
Embodiment 7 (referring to accompanying drawing 7 and accompanying drawing 11)
Present embodiment 7 is compared in embodiment 6, and ammonia-nitrogen content higher (1000～5000mg/l) and the big (＞10m of treatment capacity in waste water
3/ h) occasion, and the ammonia content in the gas can direct discharging up to standard after secondary removes ammonia, at this moment, can adopt the high dispersive spraying as the double-deck nozzle placement of the twin-stage of accompanying drawing 7 to remove ammonia+emptying tube: this tower comprises blower fan 1, air intake sparger 2, high dispersive element 3 removes ammonia Tata body 4, mist eliminator 5, riser 6 and emptying cylindrical shell 9.
Waste water is taken over through water inlet and is entered high dispersive element 3, and under 0.3～0.6MPa pressure, through nozzle 14 ejections, the nozzle direction both can upwards have been arranged also and can have been arranged downwards by minute water distributor 12; Air improves blast through blower fan 1, removes the air intlet pipe of ammonia tower from the bottom and goes into tower, is uniformly distributed in Ta Nei and upwards mobile through air intake sparger 2, and the gas ammonia that will overflow from small solution droplets is taken away rapidly, and removes the ammonia tower after riser 6 enters the middle part.Air after ammonia is removed at the two poles of the earth directly advances the discharging of emptying tube.
Embodiment 8 (referring to accompanying drawing 8 and accompanying drawing 11)
This example is the special case of embodiment 1.This example be suitable in the waste water ammonia-nitrogen content not high (＜200mg/l) and the less (3～5m of flow
3/ h) occasion.This high dispersive spraying removes the ammonia tower: comprise air intake sparger 2, high dispersive element 3 removes ammonia Tata body 4, mist eliminator 5 and induced draft fan 10.
Waste water is taken over through water inlet and is entered high dispersive element 3, and under 0.3～0.6MPa pressure, through nozzle 14 ejections, the nozzle direction both can upwards have been arranged also and can have been arranged downwards by minute water distributor 12; Air is gone into tower from removing ammonia tower bottom air intlet pipe, is uniformly distributed in Ta Nei and upwards mobile through air intake sparger 2, and the gas ammonia that will overflow from small solution droplets is taken away rapidly, takes out through induced draft fan then and draws emptying.
Embodiment 9,10 (referring to accompanying drawing 9 and accompanying drawing 10)
Fig. 9 and Figure 10 are two examples of horizontal type ammonia removal tower.This example be suitable in the waste water ammonia-nitrogen content not high (＜300mg/l) and the less (3～5m of flow
3/ h) occasion.This high dispersive spraying removes the ammonia unit, comprises air intake sparger 2, and high dispersive element 3 removes ammonia Tata body 4, mist eliminator 5.
Waste water is taken over through water inlet and is entered high dispersive element 3, and under 0.3～0.6MPa pressure, through nozzle 14 ejections, nozzle can make progress (Fig. 9) or side direction (Figure 10) is provided with by minute water distributor 12; Air advances tower by removing ammonia tower one side after blower fan boosts, flow forward behind air intake sparger uniform distribution, and the gas ammonia that will overflow from small solution droplets is taken away rapidly, enters atmosphere behind the droplet entrainment in the cat head mist eliminator.
Claims (8)
1 one kinds of high dispersive sprayings remove the ammonia tower, comprise gas blower or induced draft fan, service pump, remove ammonia Tata body and air intake sparger, it is characterized in that the high dispersive arrangements of elements is in removing ammonia Tata body, be positioned at the top of air intake sparger, the high dispersive element is by atomizing nozzle and divide water distributor to form, atomizing nozzle is provided with up or down, communicates with service pump by minute water distributor and water inlet pipe.
2, high dispersive spraying as claimed in claim 1 removes the ammonia tower, it is characterized in that removing in the ammonia Tata body mist eliminator is set, and the high dispersive element is positioned at the top of air intake sparger and the below of mist eliminator.
3, remove the ammonia tower as high dispersive spraying as described in the claim 2, it is characterized in that removing in the ammonia tower same, high dispersive element individual layer or bilayer or multilayer are arranged.
4, remove the ammonia tower as high dispersive spraying as described in claim 1 or 2 or 3, it is characterized in that the atomizing nozzle of high dispersive element links to each other with a minute water distributor by taking over, every branch water distributor is arranged several atomizing nozzles.
5, remove the ammonia tower as high dispersive spraying as described in claim 1 or 2 or 3, it is characterized in that adopting single-stage or multistage setting, or with the subsequent disposal tower with remove the stack of ammonia Tata body and arrange.
6, remove the ammonia tower as high dispersive spraying as described in the claim 4, it is characterized in that adopting single-stage or multistage setting, or with the subsequent disposal tower with remove the stack of ammonia Tata body and arrange.
7, remove the ammonia tower as high dispersive spraying as described in the claim 4, it is characterized in that described to remove ammonia Tata body be vertical, or horizontal.
8, remove the ammonia tower as high dispersive spraying as described in claim 6 or 7, it is characterized in that described to remove ammonia Tata body be steel construction piece, or concrete structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620097443 CN2937099Y (en) | 2006-06-28 | 2006-06-28 | High dispersion spray deammonia tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620097443 CN2937099Y (en) | 2006-06-28 | 2006-06-28 | High dispersion spray deammonia tower |
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| Publication Number | Publication Date |
|---|---|
| CN2937099Y true CN2937099Y (en) | 2007-08-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620097443 Expired - Lifetime CN2937099Y (en) | 2006-06-28 | 2006-06-28 | High dispersion spray deammonia tower |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102701307A (en) * | 2012-05-28 | 2012-10-03 | 江苏一环集团有限公司 | Wastewater ammonia nitrogen blow-off treatment reaction device |
| CN103964631A (en) * | 2014-03-27 | 2014-08-06 | 武汉科梦环境工程有限公司 | Efficient coal-water slurrygasification ash water treatment method |
| CN105540715A (en) * | 2016-02-03 | 2016-05-04 | 武汉兴天宇环境工程有限公司 | Ammonia removal method, ammonia removal tower and ammonia removal system |
| CN108404435A (en) * | 2018-03-08 | 2018-08-17 | 江苏师范大学 | A kind of cold concentration tower |
| CN113209654A (en) * | 2021-04-22 | 2021-08-06 | 燕山大学 | Packless pore-plate-free spray rectification bed |
-
2006
- 2006-06-28 CN CN 200620097443 patent/CN2937099Y/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102701307A (en) * | 2012-05-28 | 2012-10-03 | 江苏一环集团有限公司 | Wastewater ammonia nitrogen blow-off treatment reaction device |
| CN103964631A (en) * | 2014-03-27 | 2014-08-06 | 武汉科梦环境工程有限公司 | Efficient coal-water slurrygasification ash water treatment method |
| CN105540715A (en) * | 2016-02-03 | 2016-05-04 | 武汉兴天宇环境工程有限公司 | Ammonia removal method, ammonia removal tower and ammonia removal system |
| CN108404435A (en) * | 2018-03-08 | 2018-08-17 | 江苏师范大学 | A kind of cold concentration tower |
| CN113209654A (en) * | 2021-04-22 | 2021-08-06 | 燕山大学 | Packless pore-plate-free spray rectification bed |
| CN113209654B (en) * | 2021-04-22 | 2022-02-11 | 燕山大学 | Packless pore-plate-free spray rectification bed |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Effective date of registration: 20091019 Pledge (preservation): Pledge |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20100723 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Kemeng Sci. & Tech. Dev. Co., Ltd., Wuhan Registration number: 2009420000628 |
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| TR01 | Transfer of patent right |
Effective date of registration: 20100823 Address after: 430274 Hubei city of Wuhan province East Lake Dongxin Road Development Zone SBI Venture Street No. 2-12-1201 Patentee after: Wuhan Comeon Environment Engineering Co., Ltd. Address before: 430074, Hubei, Wuhan Road, Shandong Road, 2 blocks, 12 Patentee before: Kemeng Sci. & Tech. Dev. Co., Ltd., Wuhan |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: High dispersion spray deammonia tower Effective date of registration: 20100907 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2010990000871 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20110119 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2010990000871 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: High dispersion spray deammonia tower Effective date of registration: 20110119 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2011990000018 |
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Date of cancellation: 20111130 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2011990000018 |
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Denomination of utility model: High dispersion spray deammonia tower Effective date of registration: 20111202 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2011990000471 |
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Date of cancellation: 20130428 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2011990000471 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: High dispersion spray deammonia tower Effective date of registration: 20130428 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2013990000250 |
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Date of cancellation: 20140516 Granted publication date: 20070822 Pledgee: China Merchants Bank, Limited by Share Ltd, Wuhan, Wuchang branch Pledgor: Wuhan Comeon Environment Engineering Co., Ltd. Registration number: 2013990000250 |
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