CN113929212A - Nitrifying liquid lifting and gas releasing device and construction process thereof - Google Patents

Nitrifying liquid lifting and gas releasing device and construction process thereof Download PDF

Info

Publication number
CN113929212A
CN113929212A CN202111300559.2A CN202111300559A CN113929212A CN 113929212 A CN113929212 A CN 113929212A CN 202111300559 A CN202111300559 A CN 202111300559A CN 113929212 A CN113929212 A CN 113929212A
Authority
CN
China
Prior art keywords
cylinder
section
outer ring
thick bamboo
water inlet
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.)
Pending
Application number
CN202111300559.2A
Other languages
Chinese (zh)
Inventor
徐钊
赵嫱
杨平
陶晶
刘爽
陈凯华
黄鸽黎
崔炎炎
王潇
王超慧
李双
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Bohuite Environmental Technology Co ltd
Original Assignee
Beijing Bohuite Environmental Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beijing Bohuite Environmental Technology Co ltd filed Critical Beijing Bohuite Environmental Technology Co ltd
Priority to CN202111300559.2A priority Critical patent/CN113929212A/en
Publication of CN113929212A publication Critical patent/CN113929212A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/301Aerobic and anaerobic treatment in the same reactor

Abstract

The application relates to a nitrified liquid lifting and air releasing device and a construction process thereof, belonging to the technical field of biochemical treatment and comprising an outer ring cylinder, a central cylinder and a water inlet pipe; one end of the outer ring cylinder is closed, one end of the central cylinder penetrates through the inner part of the outer ring cylinder, the other end of the central cylinder is higher than the level of digestive juice, the central cylinder and the outer ring cylinder are coaxially arranged, the water inlet pipe is communicated with the inner part of the outer ring cylinder, and the water inlet pipe is parallel to the tangential direction of the inner wall of the outer ring cylinder; the construction process comprises the following steps: s1, assembling: assembling the outer ring barrel, the central barrel and the water inlet pipe, wherein the water inlet direction of the water inlet pipe is parallel to the tangential direction of the outer ring barrel; s2, installation: communicating one end of the water inlet pipe, which is far away from the outer ring cylinder, to the aerobic zone, so that a gap between the outer ring cylinder and the central cylinder is communicated with the anoxic zone; s3, starting: nitrifying liquid is introduced into the water inlet pipe. This application has and makes the aqueous vapor separation, guarantees that the oxygen of aquatic can not flow back to the effect in anoxic zone along with the digestive juice together.

Description

Nitrifying liquid lifting and gas releasing device and construction process thereof
Technical Field
The application relates to the technical field of biochemical treatment, in particular to a nitrified liquid lifting and air releasing device and a construction process thereof.
Background
In the current biochemical treatment system, biological denitrification is a process of finally converting nitrogen-containing compounds in water into nitrogen gas through ammoniation, nitrification and denitrification so as to be removed. Wherein the ammoniation is carried out under aerobic or anaerobic conditions, the nitrification is carried out under aerobic conditions, and the denitrification is carried out under anoxic conditions. In order to ensure the removal rate of the total nitrogen, a relatively high reflux amount of nitrifying liquid is generally needed, and the nitrifying liquid at the tail end of the aerobic zone is refluxed to the anoxic zone for denitrification.
However, the nitrified liquid carries with it a part of oxygen to enter the anoxic zone, and with the increase of the reflux amount of the nitrified liquid, the oxygen entering the anoxic zone inevitably increases, and finally, excessive oxygen destroys the anoxic environment, and inhibits the denitrification action, thus being not beneficial to removing the total nitrogen.
In view of the above-mentioned related technologies, the inventors believe that there is a defect that the nitrified liquid will carry part of the oxygen into the anoxic zone together when flowing back to the anoxic zone.
Disclosure of Invention
In order to overcome the defect that a large amount of oxygen can be carried along to enter an anoxic zone when nitrified liquid flows back to the anoxic zone, the application provides a nitrified liquid lifting and air releasing device and a construction process thereof.
In a first aspect, the application provides a nitrified liquid lifting and degassing device, which adopts the following technical scheme:
comprises an outer ring cylinder, a central cylinder and a water inlet pipe; the one end of an outer lane section of thick bamboo is sealed, the one end of a center section of thick bamboo is worn to establish inside an outer lane section of thick bamboo, the other end is higher than the digestive juice liquid level, a center section of thick bamboo and the coaxial setting of an outer lane section of thick bamboo, the inlet tube with the inside intercommunication of an outer lane section of thick bamboo, just the inlet tube with the tangential direction of an outer lane section of thick bamboo inner wall is parallel.
By adopting the technical scheme, the water outlet of the nitrified liquid lifting and air releasing device is communicated to the anoxic zone, the water inlet pipe is arranged at the bottom end of the outer ring barrel, and after sewage enters the inner part of the outer ring barrel, water entering the outer ring barrel can carry out rotational flow motion along the inner wall of the outer ring barrel under the action of centrifugal force and gradually rises; the centrifugal force is in direct proportion to the material density and the centripetal acceleration, the density of the gas in the water is far smaller than that of the water, so that the centrifugal force borne by the gas in the water can be smaller than that of the water, when the water rises to the lower end of the central cylinder, the water can continue to rise along the inner wall of the outer cylinder under the action of sufficient centrifugal force, the gas is less influenced by the centrifugal force, the flow state of the gas cannot be changed excessively, the gas can still rise according to the previous swirl amplitude and enters the inside of the central cylinder, finally, the water flows out from the top of the outer cylinder, and the gas is released from the top of the central cylinder, so that the gas-water separation is realized, the defect that a large amount of oxygen can be carried into an anoxic zone together when the nitrified liquid flows back to the anoxic zone is overcome, and the damage degree to the environment of the anoxic zone is reduced.
Optionally, a stirrer is arranged in the central cylinder, and one end of the stirrer extending into the central cylinder extends out of the lower end of the central cylinder.
Through adopting above-mentioned technical scheme, the whirl velocity of flow of water further increases under the effect of agitator, guarantees that water is keeping higher velocity of flow constantly in outer circle section of thick bamboo, and the centrifugal force that makes water receive is far greater than the centrifugal force that aquatic air received for the effect of aqueous vapor separation is better, simultaneously, through the exogenic action of agitator, for nitrifying liquid backward flow provides sufficient power, makes and need not to set up other reflux unit alone again.
Optionally, the outer circumferential surface of the center cylinder is provided with a plurality of partition plates, the plurality of partition plates are uniformly arranged along the outer circumferential surface of the center cylinder at intervals, the partition plates are arranged close to the upper end of the outer ring cylinder, one end of each partition plate is connected with the outer circumferential surface of the center cylinder, and the other end of each partition plate is connected with the inner wall of the outer ring cylinder.
Through adopting above-mentioned technical scheme, the outer wall of a center section of thick bamboo and the inner wall of an outer lane section of thick bamboo are being connected to the division board, make the division board play fixed and supported effect to a center section of thick bamboo, the stability of the device structure has been guaranteed, and simultaneously, because under the exogenic action of agitator, the rotational flow speed of water is great, it is urgent to go out the water torrent, the setting can block the water that the whirl rises at outer lane bobbin top division board, make rivers change into the steady flow state that rises from the whirl attitude, carry out the energy dissipation effect to the water, furthest's rotational flow speed of reduction water, make out more mild of water, stable.
Optionally, one end of the central cylinder, which extends out of the outer ring cylinder, is provided with a supporting device, and the supporting device is used for mounting the stirrer.
Through adopting above-mentioned technical scheme, install the agitator in central section of thick bamboo through strutting arrangement for easy operation when the agitator is installed.
Optionally, the supporting device includes a supporting frame and a supporting platform, the supporting frame is fixedly arranged on the inner wall of the central cylinder, the supporting frame includes a fixing ring and a plurality of clamping plates, the fixing ring is cylindrical, the clamping plates are evenly arranged along the inner circumferential surface of the fixing ring at intervals, the supporting platform is fixedly arranged at one end of the clamping plate far away from the fixing ring, a through hole is formed in the supporting platform, and the stirrer is arranged in the through hole in a penetrating manner.
By adopting the technical scheme, the support frame is simple in structure, easy to manufacture and cost-saving; the support frame and the support table are arranged, so that one end of the central cylinder, which extends out of the outer ring cylinder, is of an open structure, oxygen can be released from the top of the central cylinder, and the stirrer is convenient to mount.
Optionally, the lower part of the central cylinder is in a divergent trumpet shape.
Through adopting above-mentioned technical scheme for the collection that the center section of thick bamboo lower extreme can be better overflows the oxygen from the water.
Optionally, the outer ring barrel includes a first cylinder section, a divergent section, and a second cylinder section; the first cylinder section is connected with one end of the gradually expanding section, the second cylinder section is connected with the other end of the gradually expanding section, the first cylinder section, the gradually expanding section and the second cylinder section are coaxially arranged, and the cross section of the second cylinder section is larger than that of the first cylinder section.
Through adopting above-mentioned technical scheme, the diameter of first cylinder section is less for the energy that consumes when the water that enters into outer lane section of thick bamboo through the inlet tube pastes the section of thick bamboo wall whirl of first cylinder section is less, and the diameter of second cylinder section is great, makes to provide the water passing environment of big section for going out water.
Optionally, one end of the stirrer extending into the central cylinder is located at one end of the divergent section close to the first cylinder section.
By adopting the technical scheme, when water rises to the divergent section from the first cylinder section, the diameter of the divergent section is larger than that of the first cylinder section, so that the rotational flow speed of the water flow is reduced, and at the moment, the water flow still keeps a higher flow speed under the action of the external force of the stirrer.
In a second aspect, the application provides a use method of a nitrifying liquid lifting and gas releasing device, which adopts the following technical scheme:
a construction process of a nitrifying liquid lifting and gas releasing device comprises the following steps:
s1, assembling: assembling the outer ring barrel, the central barrel and the water inlet pipe, wherein the water inlet direction of the water inlet pipe is parallel to the tangential direction of the outer ring barrel;
s2, installation: communicating one end of the water inlet pipe, which is far away from the outer ring cylinder, to the aerobic zone, so that a gap between the outer ring cylinder and the central cylinder is communicated with the anoxic zone;
s3, starting: nitrifying liquid is introduced into the water inlet pipe.
Through adopting above-mentioned technical scheme, the inlet tube is intake at a high speed along the tangential direction of outer lane section of thick bamboo inner wall, make the water that gets into in the outer lane section of thick bamboo produce the whirl flow state more easily, and simultaneously, the whirl velocity of flow that makes water under the effect of agitator further increases, not only can provide sufficient power for nitrifying the liquid backward flow, can also separate air water, make the oxygen of smuggleing secretly in the nitrifying liquid release in advance, avoid excessive oxygen to follow nitrifying liquid and advance the anoxic zone together, the smooth of denitrification goes on in the anoxic zone has been guaranteed, the operation of this process is simple, and the effect is obvious.
In summary, the present application includes at least one of the following beneficial technical effects:
1. the gas-water separation is realized, the defect that a large amount of oxygen enters the anoxic zone together when the nitrified liquid flows back to the anoxic zone is overcome, and the damage degree to the environment of the anoxic zone is reduced;
2. the rotational flow velocity of water is further increased under the action of the stirrer, so that the water is kept at a higher flow velocity in the outer ring cylinder all the time, the centrifugal force borne by the water is far greater than that borne by air in the water, the water-air separation effect is better, and meanwhile, sufficient power is provided for the reflux of the nitrified liquid under the action of the external force of the stirrer, so that other reflux devices do not need to be arranged independently;
3. the device is simple to operate, convenient to install, simple to maintain and high in applicability when in use.
Drawings
FIG. 1 is a front view of an embodiment of the present application.
Fig. 2 is an exploded schematic view of an embodiment of the present application.
Fig. 3 is an enlarged schematic view of a portion a in fig. 2.
Description of reference numerals: 1. an outer ring barrel; 11. a first cylindrical section; 12. a gradual expansion section; 13. a second cylindrical section; 2. a central barrel; 21. a partition plate; 3. a water inlet pipe; 4. a support device; 41. a support frame; 411. a fixing ring; 412. clamping a plate; 42. a support table; 421. perforating; 5. a stirrer.
Detailed Description
The present application is described in further detail below with reference to figures 1-3.
The embodiment of the application discloses a nitrifying liquid lifting and air releasing device.
Referring to fig. 1, a nitrifying liquid lifting and degassing device comprises an outer ring barrel 1, a central barrel 2 arranged in the outer ring barrel 1 in a penetrating manner, and a water inlet pipe 3 arranged at the bottom end of the outer ring barrel 1; the bottom of outer lane section of thick bamboo 1 is sealed, outer lane section of thick bamboo 1 and the coaxial setting of center tube 2, inlet tube 3 and the inside intercommunication of outer lane section of thick bamboo 1, and inlet tube 3 is parallel with the tangential direction of outer lane section of thick bamboo 1 inner wall, it sets up along the tangential direction of outer lane section of thick bamboo 1 now to make inlet tube 3 interior water be whirl motion along the inner wall of outer lane section of thick bamboo 1 under the effect of centrifugal force, because the density at aquatic gas is less than the density of water, consequently the centrifugal force that aquatic gas received is less than the centrifugal force that water received, make water flow out from the top of outer lane section of thick bamboo 1, gaseous top release from center tube 2, thereby realize the separation of air water, the defect that can smuggle a large amount of oxygen together to get into the anoxic zone when having improved the nitrifying liquid and flowing back to the anoxic zone time, the destruction degree to the anoxic zone environment has been reduced.
Referring to fig. 1, the outer ring barrel 1 comprises a first cylindrical section 11, a divergent section 12 and a second cylindrical section 13; one end of the divergent section 12 is fixedly connected with one end of the first cylinder section 11, the other end of the divergent section 12 is fixedly connected with one end of the second cylinder section 13, the first cylinder section 11, the divergent section 12 and the second cylinder section 13 are coaxially arranged, one end of the first cylinder section 11 far away from the divergent section 12 is arranged as a lower end, one end of the second cylinder section 13 far away from the divergent section 12 is arranged as an upper end, and one end of the first cylinder section 11 far away from the divergent section 12 is arranged in a closed manner; the diameter of the second cylindrical section 13 is larger than that of the first cylindrical section 11, so that the second cylindrical section 13 provides a water passing environment with a large section for water outlet of the outer ring barrel 1.
Referring to fig. 1, both ends of a central cylinder 2 are arranged in an open structure, the central cylinder 2 extends into an outer ring cylinder 1 from the upper end of the outer ring cylinder 1, so that one end of the central cylinder 2 extending into the outer ring cylinder 1 is located at a divergent section 12, and the end is arranged as a divergent bell mouth, so that the lower end of the central cylinder 2 can better collect oxygen overflowing from water; the other end of the central cylinder 2 is positioned outside the outer ring cylinder 1, and one end of the central cylinder 2 extending out of the outer ring cylinder 1 is higher than the liquid level of the biochemical system.
Referring to fig. 1 and 2, the outer peripheral surface of the upper end of the central cylinder 2 is further provided with a plurality of partition plates 21, the plurality of partition plates 21 are uniformly arranged along the outer peripheral surface of the central cylinder 2 at intervals, one end of each partition plate 21 is fixedly connected with the central cylinder 2, the other end of each partition plate is fixedly connected with the inner peripheral surface of the second cylinder section 13 far away from one end of the gradually expanding section 12, so that the central cylinder 2 is fixedly arranged in the outer ring cylinder 1, the stability of the device is ensured due to the arrangement of the partition plates 21, the water flow in the outer ring cylinder 1 is changed from a swirling flow state to a stable rising flow state, the energy dissipation effect is performed on the water body, the swirling speed of the water is reduced to the maximum extent, and the water flowing out from the second cylinder section 13 is more gentle and stable.
Referring to fig. 2 and 3, the end of the central cylinder 2 extending out of the outer ring cylinder 1 is further provided with a supporting device 4, and the supporting device 4 comprises a supporting frame 41 and a supporting platform 42; the supporting frame 41 comprises a fixing ring 411 and a plurality of clamping plates 412, the fixing ring 411 is cylindrical, the outer peripheral surface of the fixing ring 411 is fixedly connected with the inner wall of one end, extending out of the outer ring barrel 1, of the central barrel 2, and the clamping plates 412 are uniformly arranged on the inner peripheral surface of the fixing ring 411 at intervals in the circumferential direction around the fixing ring 411; supporting bench 42 sets up the intermediate position at solid fixed ring 411, supporting bench 42 is circularly, supporting bench 42 and solid fixed ring 411 coaxial arrangement, cardboard 412 keeps away from solid fixed ring 411's one end and supporting bench 42's periphery fixed connection, thereby make supporting bench 42 fixed the intermediate position that sets up at solid fixed ring 411, supporting bench 42's intermediate position has still seted up perforation 421, wear to be equipped with agitator 5 in the perforation 421, agitator 5 sets up to upflow agitator 5, agitator 5's one end stretches into from perforation 421, this end stretches out central section of thick bamboo 2 and is located divergent section 12 department, agitator 5's setting makes the water that flows into in outer race section of thick bamboo 1 through inlet tube 3 under agitator 5's effect, the velocity of flow of the water of increase, make the effect of aqueous vapor separation better, and simultaneously, under agitator 5's exogenic action, still provide sufficient power for the nitration liquid backward flow.
The implementation principle of the application is as follows: the device consists of an outer ring cylinder 1, a central cylinder 2, a supporting device 4, a partition plate 21, a water inlet pipe 3 and a stirrer 5; when water enters, the water flows into the device along the tangential direction of the outer ring barrel 1 through the water inlet pipe 3, rises along the inner wall of the outer ring barrel 1 in a swirling manner, flows out of the outer side of the central barrel 2, air carried in the water is separated from the water under the action of the swirling flow and is released from the top of the central barrel 2, and the stirrer 5 is arranged in the central barrel 2 and can provide sufficient power for water inflow swirling flow and rising; this device simple to operate, maintenance are simple, when providing backward flow power for nitrifying liquid, can also carry out gas-water separation, prevent to nitrify liquid and smuggle excessive oxygen and enter into the anoxic zone secretly, are applicable to the various biochemical systems that need nitrify liquid backward flow.
The embodiment of the application also discloses a use method of the nitrification liquid lifting and air releasing device.
The method comprises the following steps:
s1, referring to the figure 1, assembling the digestive juice lifting and air releasing device; firstly, assembling an outer ring barrel 1, a central barrel 2, a supporting device 4, a partition plate 21, a water inlet pipe 3 and a stirrer 5 to form an integrated structure;
s2, referring to the figure 1, one end of the water inlet pipe 3, which is far away from the outer ring barrel 1, is communicated with the aerobic zone, so that a gap between the outer ring barrel 1 and the central barrel 2 is communicated with the anoxic zone;
s3, referring to the figure 1, the water inlet pipe 3 is used for water inlet and ensures high-speed water inlet; because the water inlet pipe 3 is arranged along the tangential direction of the inner wall of the outer ring barrel 1 and the high-speed water inlet flow speed is ensured when the water inlet pipe 3 is used for water inlet, the water flowing into the outer ring barrel 1 through the water inlet pipe 3 can more easily swirl along the inner wall of the outer ring barrel 1;
starting the stirrer 5; one end of the stirrer 5 extending into the outer ring barrel 1 is positioned at one end of the divergent section 12 close to the first cylinder section 11, when water enters the divergent section 12 from the first cylinder section 11, the diameter of the divergent section 12 is gradually increased, so that the rotational flow speed of the water is reduced, at this time, the stirrer 5 is started, the rotational flow speed of the water is continuously kept at a high flow speed through the stirrer 5, the water flows out from the upper part of the outer ring barrel 1, and the gas is released from the upper part of the central barrel 2; since the density of the gas in the water is less than that of the water, the centrifugal force to which the gas in the water is subjected is less than that to which the water is subjected, and therefore, the water continues to flow out from the upper portion of the outer ring cylinder 1 along the inner wall of the outer ring cylinder 1, and the air in the water is released from the upper portion of the center cylinder 2, thereby achieving water-gas separation.
The embodiments of the present invention are preferred embodiments of the present application, and the scope of protection of the present application is not limited by the embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.

Claims (9)

1. A nitrifying liquid lifting and gas releasing device is characterized in that: comprises an outer ring cylinder (1), a central cylinder (2) and a water inlet pipe (3); the one end of an outer ring section of thick bamboo (1) is sealed, the one end of a center section of thick bamboo (2) is worn to establish inside an outer ring section of thick bamboo (1), the other end is higher than the digestive juice liquid level, a center section of thick bamboo (2) and the coaxial setting of an outer ring section of thick bamboo (1), inlet tube (3) with the inside intercommunication of an outer ring section of thick bamboo (1), just inlet tube (3) with the tangential direction of an outer ring section of thick bamboo (1) inner wall is parallel.
2. The nitrification liquid lifting and air release device according to claim 1, wherein: a stirrer (5) is arranged in the center cylinder (2), and one end, extending into the center cylinder (2), of the stirrer (5) extends out of the lower end of the center cylinder (2).
3. The nitrification liquid lifting and air release device according to claim 1, wherein: the outer peripheral face of a center section of thick bamboo (2) is provided with polylith division board (21), the polylith division board (21) along the outer peripheral face interval of a center section of thick bamboo (2) evenly sets up, division board (21) are close to the upper end setting of outer lane section of thick bamboo (1), the one end of division board (21) with the outer peripheral face of a center section of thick bamboo (2) is connected, the other end with the inner wall connection of outer lane section of thick bamboo (1).
4. The nitrification liquid lifting and air release device according to claim 2, wherein: and one end of the central cylinder (2) extending out of the outer ring cylinder (1) is provided with a supporting device (4), and the supporting device (4) is used for installing the stirrer (5).
5. The nitrification liquid lifting and air release device according to claim 4, wherein: support arrangement (4) include support frame (41) and brace table (42), support frame (41) set firmly on the inner wall of a center section of thick bamboo (2), support frame (41) are including solid fixed ring (411) and polylith cardboard (412), gu fixed ring (411) are cylindricly, the polylith cardboard (412) along the inner peripheral surface interval of solid fixed ring (411) evenly sets up, brace table (42) set firmly cardboard (412) are kept away from the one end of solid fixed ring (411), perforation (421) have been seted up on brace table (42), agitator (5) wear to establish in perforation (421).
6. The nitrification liquid lifting and air release device according to claim 1, wherein: the lower part of the central cylinder (2) is in a gradually expanding horn shape.
7. The nitrification liquid lifting and air release device according to claim 2, wherein: the outer ring barrel (1) comprises a first cylinder section (11), a divergent section (12) and a second cylinder section (13); the first cylinder section (11) is connected with one end of the divergent section (12), the second cylinder section (13) is connected with the other end of the divergent section (12), the first cylinder section (11), the divergent section (12) and the second cylinder section (13) are coaxially arranged, and the cross section of the second cylinder section (13) is larger than that of the first cylinder section (11).
8. The nitrification liquid lifting and air release device according to claim 7, wherein: one end of the stirrer (5) extending into the central cylinder (2) is positioned at one end of the divergent section (12) close to the first cylinder section (11).
9. A construction process of a nitrifying liquid lifting and gas releasing device is characterized by comprising the following steps: the method comprises the following steps:
s1, assembling: assembling the outer ring barrel (1), the central barrel (2) and the water inlet pipe (3), wherein the water inlet direction of the water inlet pipe (3) is parallel to the tangential direction of the outer ring barrel (1);
s2, installation: one end of the water inlet pipe (3) far away from the outer ring cylinder (1) is communicated to an aerobic zone, so that a gap between the outer ring cylinder (1) and the central cylinder (2) is communicated with an anoxic zone;
s3, starting: nitrifying liquid is introduced into the water inlet pipe (3).
CN202111300559.2A 2021-11-04 2021-11-04 Nitrifying liquid lifting and gas releasing device and construction process thereof Pending CN113929212A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111300559.2A CN113929212A (en) 2021-11-04 2021-11-04 Nitrifying liquid lifting and gas releasing device and construction process thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111300559.2A CN113929212A (en) 2021-11-04 2021-11-04 Nitrifying liquid lifting and gas releasing device and construction process thereof

Publications (1)

Publication Number Publication Date
CN113929212A true CN113929212A (en) 2022-01-14

Family

ID=79285822

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111300559.2A Pending CN113929212A (en) 2021-11-04 2021-11-04 Nitrifying liquid lifting and gas releasing device and construction process thereof

Country Status (1)

Country Link
CN (1) CN113929212A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2729054Y (en) * 2004-02-20 2005-09-28 北京恩菲环保股份有限公司 Telescopic variable current whirl combined reactor
JP2011104501A (en) * 2009-11-16 2011-06-02 Mingasu:Kk Gas separation apparatus and gas separation method
CN102774962A (en) * 2012-07-20 2012-11-14 北京市环境保护科学研究院 Internal circulation hydrolysis reactor and process thereof
CN112079434A (en) * 2020-09-07 2020-12-15 天津壹新环保工程有限公司 Rural integration waste water treatment jar
CN112939218A (en) * 2021-02-05 2021-06-11 北京博汇特环保科技股份有限公司 Rotational flow backflow channel and biochemical reactor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2729054Y (en) * 2004-02-20 2005-09-28 北京恩菲环保股份有限公司 Telescopic variable current whirl combined reactor
JP2011104501A (en) * 2009-11-16 2011-06-02 Mingasu:Kk Gas separation apparatus and gas separation method
CN102774962A (en) * 2012-07-20 2012-11-14 北京市环境保护科学研究院 Internal circulation hydrolysis reactor and process thereof
CN112079434A (en) * 2020-09-07 2020-12-15 天津壹新环保工程有限公司 Rural integration waste water treatment jar
CN112939218A (en) * 2021-02-05 2021-06-11 北京博汇特环保科技股份有限公司 Rotational flow backflow channel and biochemical reactor

Similar Documents

Publication Publication Date Title
CN201343478Y (en) UASB-MBR integrated system for treating dyeing wastewater
CN210855445U (en) MABR membrane aeration bioreactor
WO2010071376A2 (en) Multi-stage air-diffusing device
CN105417881A (en) Self-circulating biological membrane denitrifying sewage treatment equipment
CN216273330U (en) Nitrifying liquid lifting and gas releasing device
CN113929212A (en) Nitrifying liquid lifting and gas releasing device and construction process thereof
CN212609804U (en) MBR aeration equipment
KR20120028554A (en) Waste water treatment apparatus which uses magnetization treatment and media porous trommel
CN213060364U (en) Nitrogen and phosphorus removal contact oxidation sewage treatment device
CN107651753B (en) Sewage denitrification and dephosphorization device
CN214829318U (en) Rotational flow backflow channel and biochemical reactor
CN205241467U (en) Self -circulation biomembrane denitrogenation sewage treatment device
CN101973665A (en) A/O reactor with functions of air lift, backflow as well as rotation and mixing of reflux
JP2003080286A (en) Water treatment equipment and screen for the same
CN112939218A (en) Rotational flow backflow channel and biochemical reactor
CN214990937U (en) Sewage treatment ecosystem with multistage aeration tank
CN111847765A (en) District sewage integration high efficiency processing system
CN220618644U (en) Integral type anaerobic ammonia oxidation equipment
CN220845847U (en) Denitrification and dephosphorization reactor based on rural domestic sewage
CN220413060U (en) Integral type AO reactor
CN220078799U (en) Circulation AO integration sewage treatment plant
CN113968622B (en) Inversion type multi-ring flow micro-power aerobic granular sludge water treatment device
CN216808353U (en) Efficient screening and separating system for granulated microorganism aggregates
CN112573773A (en) Sewage treatment ecosystem with multistage aeration tank
CN213865575U (en) MBR membrane biological reaction sewage treatment plant

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination