CN200974794Y - Seawater desulfurizing deep well aeration device - Google Patents
Seawater desulfurizing deep well aeration device Download PDFInfo
- Publication number
- CN200974794Y CN200974794Y CNU2005200983235U CN200520098323U CN200974794Y CN 200974794 Y CN200974794 Y CN 200974794Y CN U2005200983235 U CNU2005200983235 U CN U2005200983235U CN 200520098323 U CN200520098323 U CN 200520098323U CN 200974794 Y CN200974794 Y CN 200974794Y
- Authority
- CN
- China
- Prior art keywords
- seawater
- aeration
- downtake
- upcast
- intake
- 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
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Treating Waste Gases (AREA)
Abstract
A flue gas seawater desulfuration deep tunnel aeration device consists essentially of a seawater intake, a downcomer, a mixed intake, an air intake, an ascension pipe and a seawater outlet. When the aeration seawater is added into the downcomer via seawater intake, the mixed seawater is added into the downcomer via the mixed intake. After the aeration seawater is mixed with the mixed seawater during the process of the down flowing, the sulfur dioxide in the aeration seawater is converted into sulfite. The air with pressure is added into the downcomer via air intake and continues flowing downwards, and then flows upwards in the ascension pipe. With contact with seawater deeper than thirty meters and the diffusion in the water, the oxygen in the air dissolves into the seawater efficiently and oxidizes the sulfite into sulfate, releasing carbon dioxide. The quality-recovered seawater is drained out when coming to the outlet. The seawater desulfuration deep tunnel aeration device has advantages of low investment, less land occupation, remarkable energy saving and high aeration efficiency.
Description
Affiliated technical field
The utility model relates to a kind of flue gas sea water desulfuration aerating apparatus, is applicable to that the heat-engine plant desulfurized minimizing aeration that cuts down the consumption of energy in beach accounts for the aerating apparatus in place.
Background technology
The aeration of beach flue gas desulphurization normally adopts perforated pipe aerating regulation or other conventional aerating apparatuss now.Not only coefficient of oxygen utilization is low, the need gas consumption is big, energy consumption is high, facility is complicated for these aerating apparatuss, also will build the no small aeration tank of occupation of land, and this is heat-engine plant desulfurized to very nervous beach, land for building to be a no small burden.
Goal of the invention
The purpose of this utility model provides a kind of seawater aeration new device, can significantly improve coefficient of oxygen utilization, significantly cut down the consumption of energy, make the no small aeration tank of occupation of land to become the aeration vertical shaft that takes up little room, and significantly reduced construction cost, also significantly reduced working cost.
Summary of the invention
Principle of work of the present utility model is, the solubleness of the solubleness of oxygen in water under the normal pressure under the high pressure; The aeration vertical shaft takes up an area of few, and fabrication cost is low.
The purpose of this utility model is achieved in that in underground construction as well downtake and upcast, at deep under ground, downtake and upcast two pipes link.Seawater ginseng hybrid junction mouth and aeration air interface are set at the middle part of downtake, after the seawater for the treatment of aeration enters from the upper inlet of downtake, down mixing sea water mixing with the ginseng that enters into downtake in the flow process, treat that the Sulphur Dioxide in the seawater of aeration becomes sulphite, because the air that ginseng is mixed is in underground deep water mesohigh place, the solubleness of oxygen solubility under the normal pressure, and make the sulphite that is dissolved in the seawater change into vitriol rapidly, and emit carbonic acid gas, the seawater that ginseng has been mixed air continues aeration and rises mobile through downtake and the upcast two pipes back, place that links, after flowing out upcast, carbonic acid gas enters in the air, and the seawater that recovers water quality is discharged to the extra large pipe from the aeration mouth of pipe.
Beneficial effect
Because far above conventional aeration pressure, the amount that the airborne oxygen of aeration dissolves in the seawater compares conventional high times, and actual aeration air quantity is significantly reduced in pipe bottom water depth pressure, it is very remarkable to economize on electricity; The construction cost of downtake and upcast also is lower than the aeration tank simultaneously, and its floor space is also few.
Description of drawings: the utility model is further specified below in conjunction with accompanying drawing.
Fig. 1. be the deep-wall type aeration yarn system of the concentric structure of downtake in upcast.
Fig. 2. being downtake is being the deep-wall type aeration yarn system of U type tubular construction with upcast.
Label in the accompanying drawing: seawater inlet (1), downtake (2), ginseng is sneaked into mouthful (3), gas inlet (4), upcast (5), tube wall (6), earth (7), seawer outlet (8), downtake (9), upcast (10).
At Fig. 1. middle downtake (2) in upcast (5) and two pipes coaxial, when the seawater of desiring aeration flows downward after seawater inlet (1) enters in the downtake (2); The sulfurous gas that is dissolved in the seawater during for fear of the washing flue gas is overflowed from seawater, be provided with ginseng at downtake (2) nearby from aeration seawater inlet (1) and sneak into mouthful (3), ginseng is mixed seawater and is added through this, thereby increased the alkalinity in the seawater, convert the sulfurous gas that is dissolved in the seawater to sulphite, and continue to flow downward.The Geng Xiachu that sneaks into mouthful (3) in ginseng is provided with gas inlet (4),, and is spread apart in the seawater that flows downward again in this joins downtake (2) by the air of Aeration fan force feed fork-like farm tool used in ancient China.Since the seawater place that has blasted air from upper orifice have more than ten meter dark, reach tens meters down deeplyer, therefore the oxygen that is dissolved in the seawater exceeds more than ten times than routine, sulphite in the seawater just can convert vitriol to fully the way of upcast (6) of flowing through again from the lower port outflow of downtake (2), and emit carbonic acid gas, the seawater of discharging from aeration seawer outlet (8) is the seawater of complete allow compliance with emission standards.
At Fig. 2. middle basic condition and Fig. 1. in 8 identical, just upcast and downtake is not concentric structure but by upcast (9) and downtake (10) formation U type structure.
Claims (2)
1. flue gas sea water desulfuration deep well aeration device, by seawater inlet (1), downtake (2), ginseng is sneaked into mouthful (3), gas inlet (4), upcast (5), seawer outlet compositions such as (8), it is characterized in that: downtake and upcast have the degree of depth greater than 30 meters underground, seawater inlet (1) upper surface of (2) in downtake, ginseng is sneaked into the middle and upper part that mouthful (3) are connected on downtake (2), the middle and upper part ginseng that gas inlet (4) is connected on downtake (2) sneak into mouthful (3) below, the lower surface mouth of pipe UNICOM of downtake (2) and upcast (5), upcast (5) the upper surface mouth of pipe connects seawer outlet (8) and UNICOM's atmosphere.
2. according to the described sea water desulfuration deep well aeration of claim 1. device, it is characterized in that downtake with upcast both can be the downtake (2) of coaxial inner conductor and the sleeve structure of upcast (5), also can downtake (9) with upcast (10) two pipe bottoms link the U tubular construction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2005200983235U CN200974794Y (en) | 2005-10-11 | 2005-10-11 | Seawater desulfurizing deep well aeration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2005200983235U CN200974794Y (en) | 2005-10-11 | 2005-10-11 | Seawater desulfurizing deep well aeration device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN200974794Y true CN200974794Y (en) | 2007-11-14 |
Family
ID=38901084
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNU2005200983235U Expired - Fee Related CN200974794Y (en) | 2005-10-11 | 2005-10-11 | Seawater desulfurizing deep well aeration device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN200974794Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102515344A (en) * | 2011-12-31 | 2012-06-27 | 山东汇盛天泽环境工程有限公司 | High-load vertical ultradeep bioreactor |
CN102775007A (en) * | 2012-07-06 | 2012-11-14 | 徐旭 | Method and device for treating sewage |
-
2005
- 2005-10-11 CN CNU2005200983235U patent/CN200974794Y/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102515344A (en) * | 2011-12-31 | 2012-06-27 | 山东汇盛天泽环境工程有限公司 | High-load vertical ultradeep bioreactor |
CN102515344B (en) * | 2011-12-31 | 2013-12-04 | 山东汇盛天泽环境工程有限公司 | High-load vertical ultradeep bioreactor |
CN102775007A (en) * | 2012-07-06 | 2012-11-14 | 徐旭 | Method and device for treating sewage |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106115950A (en) | A kind of over-saturation dissolved oxygen aerator | |
CN201087142Y (en) | Solid-liquid separation gas dissolving device | |
CN104150720B (en) | Air lift type integrated sewage treatment device | |
CN103212348B (en) | A kind of oxidation technology of ammonium sulfite and device | |
CN200974794Y (en) | Seawater desulfurizing deep well aeration device | |
CN102139951A (en) | Rotational flow shearing bubble aerator | |
CN211571646U (en) | Air supply ridge structure for drainage energy dissipation hole | |
CN107500443A (en) | Novel desulfurization seawater aeration device and method | |
CN205953680U (en) | Super supersaturated with dissolved oxygen aeration equipment | |
CN200957338Y (en) | Series absorber of impact levelling thrust | |
CN207175701U (en) | A kind of livestock breeding wastewater integrated treatment unit | |
CN212334746U (en) | Anaerobic reactor for wastewater treatment | |
CN206156839U (en) | Bed of packings efflux aeration tank | |
CN209685716U (en) | The simple collection and purification storing and conveying device of biogas | |
CN204400701U (en) | Siphon gas injection type is wandered about as a refugee biochemical process Sewage treatment systems | |
CN105417682B (en) | A kind of reoxygenation devices and methods therefor of unpowered river surface water | |
CN217947720U (en) | Air stripping device | |
CN111717990A (en) | Anaerobic reactor for wastewater treatment and method for treating wastewater | |
CN201854608U (en) | Water lifting and pushing aeration oxygen-enhanced device based on gas jet | |
CN107720933B (en) | Ozone contact reaction water treatment device and method | |
CN201525772U (en) | Carbon dioxide removing device in mineral water production | |
CN205442804U (en) | Reoxygenation device of unpowered river surface water | |
CN106430587B (en) | Two stages automatic stirring sewage clean water tank with denitrification functions | |
CN214457179U (en) | River oxygenation equipment and control system thereof | |
CN109825340A (en) | The simple collection and purification storing and conveying device and method of biogas |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
DD01 | Delivery of document by public notice |
Addressee: Yu Hanming Document name: Notification to Pay the Fees |
|
DD01 | Delivery of document by public notice |
Addressee: Yu Hanming Document name: Notification of Termination of Patent Right |
|
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071114 Termination date: 20111011 |