CN115253387A - Ammonia stripping cabinet and ammonia stripping method - Google Patents

Ammonia stripping cabinet and ammonia stripping method Download PDF

Info

Publication number
CN115253387A
CN115253387A CN202210970097.3A CN202210970097A CN115253387A CN 115253387 A CN115253387 A CN 115253387A CN 202210970097 A CN202210970097 A CN 202210970097A CN 115253387 A CN115253387 A CN 115253387A
Authority
CN
China
Prior art keywords
dosing
cabinet body
cabinet
ammonia stripping
pipeline
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.)
Granted
Application number
CN202210970097.3A
Other languages
Chinese (zh)
Other versions
CN115253387B (en
Inventor
徐玉森
李华伟
王宏武
张晓威
蔺洪永
王亚辉
马萌萌
秦菊芬
杜维
徐杰
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.)
Central Plains Environmental Protection Co ltd
Original Assignee
Central Plains Environmental Protection 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 Central Plains Environmental Protection Co ltd filed Critical Central Plains Environmental Protection Co ltd
Priority to CN202210970097.3A priority Critical patent/CN115253387B/en
Publication of CN115253387A publication Critical patent/CN115253387A/en
Application granted granted Critical
Publication of CN115253387B publication Critical patent/CN115253387B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Water Treatments (AREA)
  • Degasification And Air Bubble Elimination (AREA)

Abstract

The invention provides an ammonia stripping cabinet and an ammonia stripping method, wherein the ammonia stripping cabinet comprises a cabinet body, an alkali liquor container and an aeration device, the cabinet body is of an asymmetric square structure, a containing cavity is formed inside the cabinet body, ammonia nitrogen solution to be treated is contained in the containing cavity, the cabinet body is provided with a water inlet, a water outlet and a gas outlet which are communicated with the containing cavity, the water inlet and the water outlet are arranged on two opposite sides of the bottom of the cabinet body, and the gas outlet is arranged at the top of the cabinet body; the alkali liquor container is filled with alkali liquor and is communicated with the cabinet body through a dosing pipeline; the aeration device is arranged at the bottom of the accommodating cavity, is communicated with the outside air and is used for aerating the solution in the accommodating cavity. The ammonia stripping tower adopts the structure of the ammonia stripping cabinet, can effectively solve the problems of high power consumption, low stripping efficiency, high investment, hardening of filler for a long time and high maintenance risk degree of the existing ammonia stripping tower, and has the advantages of convenient operation, low power consumption, stripping efficiency of more than 80 percent and higher stripping efficiency than the ammonia stripping tower.

Description

Ammonia stripping cabinet and ammonia stripping method
Technical Field
The invention belongs to the technical field of ammonia stripping, and particularly relates to an ammonia stripping cabinet and an ammonia stripping method.
Background
The basic principle of ammonia stripping is that air is used for stripping under an alkaline condition by utilizing the difference between the actual concentration and the equilibrium concentration of volatile substances such as ammonia nitrogen and the like contained in a solution, and the concentration of ammonia in a gas phase is changed due to continuous gas discharge in the stripping process, so that the actual concentration of the ammonia is always smaller than the equilibrium concentration under the condition, and finally, ammonia dissolved in the solution continuously passes through a gas-liquid interface, so that the ammonia Nitrogen (NH) in the solution 3 -N) are removed. At present, a cylindrical ammonia stripping tower is mostly adopted by an ammonia stripping device, the height-diameter ratio of the tower is 6-1, the process is mature, the operation is simple, the stripping efficiency can reach 60-70% in a single stage, however, the power consumption of the ammonia stripping tower is large, the stripping efficiency is further improved, the investment is large, the equipment is too high, the packing is hardened for a long time, and the overhaul risk degree is high.
Therefore, there is a need to provide an improved solution to the above-mentioned deficiencies of the prior art.
Disclosure of Invention
The invention aims to provide an ammonia stripping cabinet and an ammonia stripping method, and aims to solve the problems of high power consumption, low stripping efficiency, high investment, hardening of fillers for a long time and high overhauling risk degree of the existing ammonia stripping tower.
In order to achieve the above purpose, the invention provides the following technical scheme:
an ammonia stripping cabinet, comprising:
the ammonia nitrogen treatment device comprises a cabinet body, a first treatment device and a second treatment device, wherein the cabinet body is of an asymmetric square structure, a containing cavity is formed inside the cabinet body, ammonia nitrogen solution to be treated is contained in the containing cavity, the cabinet body is provided with a water inlet, a water outlet and a gas outlet which are communicated with the containing cavity, the water inlet and the water outlet are arranged on two opposite sides of the bottom of the cabinet body, and the gas outlet is arranged at the top of the cabinet body;
the alkali liquor container is filled with alkali liquor and communicated with the cabinet body through a dosing pipeline;
and the aeration device is arranged at the bottom of the accommodating cavity, is communicated with the outside air and is used for aerating the solution in the accommodating cavity.
Optionally, the cabinet body is of an asymmetric square structure with a high left side and a low right side, and the height of the left side is 1.5-2 times of the height of the right side; the gas outlet is arranged at the top of the left side of the cabinet body.
Optionally, the water outlet is connected with a water outlet pipe, the water outlet end of the water outlet pipe is higher than the water outlet, the depth of the ammonia nitrogen solution is the same as the height of the water outlet end of the water outlet pipe, and the depth of the ammonia nitrogen solution is not less than 2/3 of the height of the right side of the cabinet body.
Optionally, the water inlet is connected with a water inlet pipe, the water inlet pipe is provided with a first dosing port, and the bottom of the cabinet body is also provided with a second dosing port and a third dosing port at intervals;
the drug adding pipeline comprises a first drug adding pipeline, a second drug adding pipeline and a third drug adding pipeline;
the alkali liquor container is connected with a liquid outlet pipe, a four-way valve is arranged on the liquid outlet pipe, of three outlets of the four-way valve, a first outlet is connected with the first dosing port through the first dosing pipe, a second outlet is connected with the second dosing port through the second dosing pipe, a third outlet is connected with the third dosing port through the third dosing pipe, and each dosing pipeline is provided with a metering pump.
Optionally, a first inserting opening and a second inserting opening are further formed in the bottom of the cabinet body, the first inserting opening is located between the water inlet and the second dosing opening, the second inserting opening is located between the second dosing opening and the third dosing opening, and the water outlet pipe is provided with a third inserting opening;
the ammonia stripping cabinet further comprises a first pH meter, a second pH meter and a third pH meter which are respectively inserted and fixed in the first inserting opening, the second inserting opening and the third inserting opening and used for detecting the pH value of the solution at the corresponding position.
Optionally, the ammonia stripping cabinet further comprises a PLC controller, and the first pH meter, the second pH meter, the third pH meter, the four-way valve and the metering pump on each dosing pipeline are electrically connected to the PLC controller through wires.
Optionally, the aeration device includes a fan, a plurality of aeration heads and a plurality of intake pipes, the import of fan and outside air intercommunication, it is a plurality of aeration head interval set up in the bottom in holding chamber, it is a plurality of intake pipe correspond connect in a plurality of aeration head, and all with the exit linkage of fan.
The invention also provides an ammonia stripping method, which adopts the ammonia stripping cabinet and comprises the following steps:
respectively conveying an ammonia nitrogen solution and an alkali liquor to an accommodating cavity of a cabinet body through a water inlet and a medicine adding pipeline, and simultaneously starting an aeration device;
and step two, detecting the pH values of the solutions at different positions in the cabinet body, and controlling the drug adding pipeline to be switched on and off and the drug adding frequency according to the detected pH values.
Optionally, in the first step, controlling the gas-liquid ratio to be 800.
Optionally, the second step is specifically:
when the reading of the first pH meter is less than 11, a metering pump on the first dosing pipeline is opened, the four-way valve correspondingly opens the first dosing pipeline, and the dosing frequency is increased until the reading of the first pH meter is not less than 11;
when the reading of the second pH meter is less than 10, the metering pump on the second dosing pipeline is opened, the four-way valve correspondingly opens the second dosing pipeline, and the dosing frequency is increased until the reading of the second pH meter is not less than 10;
and when the reading of the third pH meter is less than 9, the metering pump on the third dosing pipeline is opened, the four-way valve correspondingly opens the third dosing pipeline, and the dosing frequency is increased until the reading of the third pH meter is between 8.5 and 9.
Has the beneficial effects that:
the ammonia stripping cabinet comprises a cabinet body, an alkali liquor container and an aeration device, wherein the cabinet body is of an asymmetric square structure, a containing cavity is formed inside the cabinet body, an ammonia nitrogen solution to be treated is contained in the containing cavity, the cabinet body is provided with a water inlet, a water outlet and a gas outlet which are communicated with the containing cavity, the water inlet and the water outlet are arranged on two opposite sides of the bottom of the cabinet body, and the gas outlet is arranged at the top of the cabinet body; the alkali liquor container is filled with alkali liquor and communicated with the cabinet body through a dosing pipeline; aeration equipment sets up in the bottom in holding chamber to communicate with the outside air, be used for carrying out the aeration to the solution of holding intracavity. The ammonia stripping tower adopts the structure of the ammonia stripping cabinet, and can effectively solve the problems of high power consumption, low stripping efficiency, high investment, hardening of fillers for a long time and high overhauling risk degree of the existing ammonia stripping tower.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of this specification, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate exemplary embodiments of the invention and together with the description serve to explain the invention and not to limit the invention. Wherein:
FIG. 1 is a schematic structural diagram of an ammonia stripping cabinet according to the present invention.
The reference numbers in the figures: 1-a cabinet body; 11-a water inlet pipe; 12-a water outlet pipe; 13-an air outlet pipe; 2-an aeration head; 21-an air inlet pipe; 3, a fan; 31-a fan switch valve; 4-an alkali liquor container; 41-a first medicated pipeline; 41 a-first metering pump; 42-a second dosing pipeline; 42 a-a second metering pump; 43-a third dosing pipeline; 43 a-a third metering pump; 44-a four-way valve; 5-a PLC controller; 51-a first pH meter; 52-a second pH meter; 53 third pH meter.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely below, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments that can be derived by one of ordinary skill in the art from the embodiments given herein are intended to be within the scope of the present invention.
The present invention will be described in detail with reference to examples. It should be noted that the embodiments and features of the embodiments may be combined with each other without conflict.
The invention provides an ammonia stripping cabinet, which adopts the structural arrangement of the ammonia stripping cabinet, and can effectively solve the problems of large power consumption, low stripping efficiency, large investment, hardening of filler for a long time and high overhauling risk degree of the existing ammonia stripping tower.
As shown in fig. 1, the ammonia stripping cabinet of the present invention comprises a cabinet body 1, an alkali liquor container 4 and an aeration device, wherein the cabinet body 1 is an asymmetric square structure, a holding cavity is formed inside the cabinet body, the holding cavity holds an ammonia nitrogen solution to be treated, the cabinet body 1 is provided with a water inlet, a water outlet and a gas outlet which are communicated with the holding cavity, the water inlet and the water outlet are arranged on two opposite sides of the bottom of the cabinet body 1, the gas outlet is arranged on the top of the cabinet body 1, and the water inlet is used for conveying the ammonia nitrogen solution to be treated into the cabinet body 1; the alkali liquor container 4 is internally provided with alkali liquor, the alkali liquor container 4 is communicated with the cabinet body 1 through a medicine adding pipeline, and the alkali liquor can be conveyed into the cabinet body 1 through the medicine adding pipeline; aeration equipment sets up in the bottom in holding chamber to communicate with the outside air, be used for carrying out the aeration to the solution of holding intracavity.
It should be noted that the lye container can be selected as a lye tank, a lye barrel and the like, the lye can be selected as a sodium hydroxide solution with the mass concentration of 30%, the gas outlet can be connected with an air outlet pipe 13, and the air outlet pipe 13 is connected with a gas absorption device and can be used for absorbing gas released by stripping so as to avoid the pollution of the gas to the outside air. The structure of the gas absorption device is not limited, and the existing conventional ammonia gas absorption device can be adopted.
The working principle of the ammonia stripping cabinet is as follows: after ammonia nitrogen solution mixes with alkali lye (for example sodium hydroxide) in the cabinet body 1, can produce a large amount of ammonia immediately, blow off at aeration equipment's aeration (air), the mixture of ammonia and air can leave the solution fast, finally discharges by the gas outlet at cabinet body 1 top, so alright realize blowing off fast of ammonia nitrogen solution. The arrows in fig. 1 indicate the gas flow direction.
In the embodiment of the invention, the cabinet body 1 has an asymmetric square structure with a high left side and a low right side, and the height of the left side is 1.5-2 times (for example, 1.5 times, 1.6 times, 1.7 times, 1.8 times, 1.9 times, 2 times and the interval value between any two end point values) of the height of the right side; the gas outlet sets up the left side top of the cabinet body 1, such structural design, can be more abundant and more effectively with the gas that blows off in the cabinet body 1 discharge by the gas outlet. It should be noted that the water inlet is located at the bottom of the left side of the cabinet body 1, and the water outlet is located at the bottom of the right side of the cabinet body 1.
In the embodiment of the invention, the water outlet is connected with a water outlet pipe 12, the water outlet end of the water outlet pipe 12 is higher than the water outlet, the depth of the ammonia nitrogen solution is the same as the height of the water outlet end of the water outlet pipe 12, and the depth of the ammonia nitrogen solution is not less than 2/3 of the height of the right side of the cabinet body 1. That is, the water outlet pipe 12 is raised to a certain height from the bottom of the cabinet body 1, and the raised height is the same as the depth of the ammonia nitrogen solution in the cabinet body 1. The setting of so structure can guarantee that the abundant effectual air-stripping that blows of the interior ammonia nitrogen solution of the cabinet body 1 to avoid it to take place the phenomenon of short stream, also guarantee simultaneously that the time that the ammonia molecule exists should not overlong in solution.
Optionally, the depth of the ammonian solution is 500mm, and the height of the water outlet end of the water outlet pipe 12 is also 500mm.
In the specific embodiment of the invention, the water inlet is connected with a water inlet pipe 11, the water inlet pipe 11 is provided with a first dosing port, and the bottom of the cabinet body 1 is also provided with a second dosing port and a third dosing port at intervals; the medicine adding pipelines comprise a first medicine adding pipeline 41, a second medicine adding pipeline 42 and a third medicine adding pipeline 43; alkali lye container 4 is connected with the drain pipe, be provided with cross valve 44 on the drain pipe, in the three export of cross valve 44, first export is through first dosing union coupling in first dosing mouth, second export is through second dosing union coupling in second dosing mouth, the third export is through third dosing union coupling in third dosing mouth, all be provided with the measuring pump on each dosing pipeline, be provided with first measuring pump 41a on first dosing pipeline 41 promptly, be provided with second measuring pump 42a on the second dosing pipeline 42, be provided with third measuring pump 43a on the third dosing pipeline 43. The design can realize that the ammonia nitrogen solution in the cabinet body 1 is added with the medicine through three medicine pipelines, and can independently add the medicine operation each other.
Preferably, the second dosing port and the third dosing port are uniformly distributed at the bottom of the cabinet body 1, so as to more fully and uniformly perform dosing operation.
The independent medicine feeding operation of three medicine feeding pipelines is realized through setting up four-way valve 44 in this embodiment, of course, in some other embodiments, can be that corresponding control valve is set up respectively on three medicine feeding pipelines to realize its independent medicine feeding operation.
Further, a first inserting opening and a second inserting opening are further formed in the bottom of the cabinet body 1, the first inserting opening is located between the water inlet and the second dosing opening, and preferably, the first inserting opening is close to the second dosing opening; the second inserting opening is positioned between the second dosing opening and the third dosing opening, and preferably, the second inserting opening is arranged close to the third dosing opening; the water outlet pipe 12 is provided with a third inserting opening; the ammonia stripping cabinet further comprises a first pH meter 51, a second pH meter 52 and a third pH meter 53 which are respectively inserted and fixed in the first insertion opening, the second insertion opening and the third insertion opening and are used for detecting the pH value of the solution at the corresponding positions.
Further, the ammonia stripping cabinet further comprises a PLC controller 5, and the first pH meter 51, the second pH meter 52, the third pH meter 53, the four-way valve 44 and the metering pumps on each dosing pipeline are electrically connected to the PLC controller 5 through wires. With such a design, the PLC controller 5 can automatically obtain the readings of the first pH meter 51, the second pH meter 52, and the third pH meter 53, and automatically control the four-way valve 44 and the switching operation of the metering pumps on each dosing pipeline, thereby realizing automatic control.
In the embodiment of the invention, the aeration device comprises a fan 3, a plurality of aeration heads 2 and a plurality of air inlet pipes 21, wherein an inlet of the fan 3 is communicated with the outside air, the plurality of aeration heads 2 are arranged at the bottom of the accommodating cavity at intervals, and the plurality of air inlet pipes 21 are correspondingly connected with the plurality of aeration heads 2 and are all connected with an outlet of the fan 3.
Specifically, as shown in fig. 1, an inlet of the blower 3 is communicated with the outside air through a pipe, and a blower switching valve 31 is provided on the pipe for controlling the circulation or non-circulation of the pipe. Optionally, the fan switch valve 31 is electrically connected to the PLC controller 5 through a wire, so as to implement an automatic control operation. A plurality of aeration heads 2 and a corresponding plurality of air inlet pipes 21 are arranged in parallel and connected to the outlet of the fan 3 through a main pipe. The aeration head 2 of the embodiment adopts a rubber film corundum aeration head 2.
The invention also provides an ammonia stripping method, which adopts the ammonia stripping cabinet and comprises the following steps:
step one, respectively conveying ammonia nitrogen solution and alkali liquor to the accommodating cavity of the cabinet body 1 through a water inlet and a dosing pipeline, and simultaneously starting an aeration device. Specifically, carry ammonia nitrogen solution and alkali lye to the holding intracavity of the cabinet body 1 respectively through inlet tube 11 and three medicine pipeline, open fan control valve 31 simultaneously, with the outside air intercommunication, open fan 3, alright carry out the aeration operation to the holding intracavity solution of the cabinet body 1 through fan 3, intake pipe 21 and aeration head 2.
In the specific embodiment of the invention, in the first step, the gas-liquid ratio is controlled to be 800.
And step two, detecting the pH values (namely the readings of different pH meters) of the solutions at different positions in the cabinet body 1, and controlling the drug adding pipeline switch and the drug adding frequency according to the detected pH values.
The second step is specifically as follows: when the reading of the first pH meter 51 is less than 11, the metering pump on the first dosing pipeline 41 (i.e. the first metering pump 41 a) is turned on, and the four-way valve 44 correspondingly turns on the first dosing pipeline 41, i.e. the first dosing pipeline 41 is conducted, and simultaneously the circulation of the second dosing pipeline 42 and the third dosing pipeline 43 is blocked, and the dosing frequency is increased by 0.5Hz; until the indication of the first pH meter 51 is not less than 11;
when the reading of the second pH meter 52 is less than 10, the metering pump on the second dosing pipeline 42 (i.e. the second metering pump 42 a) is turned on, and the four-way valve 44 correspondingly turns on the second dosing pipeline 42, i.e. the second dosing pipeline 42 is conducted, and simultaneously the circulation of the first dosing pipeline 41 and the third dosing pipeline 43 is blocked, and the dosing frequency is increased by 0.5Hz; until the index of the second pH meter 52 is not less than 10;
when the indication number of the third pH meter 53 is less than 9, the metering pump (i.e., the third metering pump 43 a) on the third dosing pipeline 43 is turned on, and the four-way valve 44 correspondingly turns on the third dosing pipeline 43, i.e., the third dosing pipeline 43 is conducted, and simultaneously the circulation of the first dosing pipeline 41 and the second dosing pipeline 42 is blocked, and the dosing frequency is increased by 0.5Hz; until the indication of the third pH meter 53 is between 8.5 and 9;
and detecting and adjusting once every 10-12min (such as 10min, 11min, 12min and interval values between any two endpoint values) according to the sequence.
By adopting the design, the maximum stripping efficiency can be kept. The ammonia nitrogen concentration when the export section is very low, the mist of air and ammonia nitrogen, it is relative with the rivers direction, on left side solution surface, with the gas mixing of the ammonia nitrogen concentration of relative height, thereby make ammonia nitrogen concentration descend, according to henry's theorem, this ammonia nitrogen that is favorable to the solution of its lower part can be sent out, the gas flow of whole cabinet body 1, all be solution ammonia nitrogen's the spilling over with higher speed, proper amount at this moment replenishes sodium hydroxide, can make the ammonia nitrogen spill over more easily.
In the concrete embodiment of the invention, the ammonia stripping pilot test is carried out by adopting the ammonia stripping cabinet, the ammonia nitrogen concentration of inlet water is 13600mg/L, the gas-liquid ratio is 1000.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (10)

1. An ammonia stripping cabinet, characterized in that the ammonia stripping cabinet comprises:
the ammonia nitrogen treatment cabinet comprises a cabinet body, wherein the cabinet body is of an asymmetric square structure, an accommodating cavity is formed inside the cabinet body, ammonia nitrogen solution to be treated is accommodated in the accommodating cavity, the cabinet body is provided with a water inlet, a water outlet and a gas outlet which are communicated with the accommodating cavity, the water inlet and the water outlet are arranged on two opposite sides of the bottom of the cabinet body, and the gas outlet is arranged at the top of the cabinet body;
the alkali liquor container is filled with alkali liquor and is communicated with the cabinet body through a medicine feeding pipeline;
and the aeration device is arranged at the bottom of the accommodating cavity, is communicated with the outside air and is used for aerating the solution in the accommodating cavity.
2. The ammonia stripping cabinet as claimed in claim 1, wherein the cabinet body is an asymmetric square structure with a height from left to right, and the height of the left side is 1.5-2 times of the height of the right side;
the gas outlet is arranged at the top of the left side of the cabinet body.
3. The ammonia stripping cabinet according to claim 2, wherein the water outlet is connected with a water outlet pipe, the water outlet end of the water outlet pipe is higher than the water outlet, the depth of the ammonia nitrogen solution is the same as the water outlet end of the water outlet pipe, and the depth of the ammonia nitrogen solution is not less than 2/3 of the right side of the cabinet body.
4. The ammonia stripping cabinet as claimed in claim 3, wherein the water inlet is connected with a water inlet pipe, the water inlet pipe is provided with a first dosing port, and the bottom of the cabinet body is further provided with a second dosing port and a third dosing port at intervals;
the drug adding pipeline comprises a first drug adding pipeline, a second drug adding pipeline and a third drug adding pipeline;
the alkali liquor container is connected with a liquid outlet pipe, a four-way valve is arranged on the liquid outlet pipe, of three outlets of the four-way valve, a first outlet is connected with the first dosing port through the first dosing pipe, a second outlet is connected with the second dosing port through the second dosing pipe, a third outlet is connected with the third dosing port through the third dosing pipe, and each dosing pipeline is provided with a metering pump.
5. The ammonia stripping cabinet according to claim 4, wherein a first inserting opening and a second inserting opening are further formed in the bottom of the cabinet body, the first inserting opening is located between the water inlet and the second dosing opening, the second inserting opening is located between the second dosing opening and the third dosing opening, and the water outlet pipe is provided with a third inserting opening;
the ammonia stripping cabinet further comprises a first pH meter, a second pH meter and a third pH meter which are respectively inserted and fixed in the first inserting opening, the second inserting opening and the third inserting opening and used for detecting the pH value of the solution at the corresponding position.
6. The ammonia stripping cabinet according to claim 5, further comprising a PLC controller, wherein the first pH meter, the second pH meter, the third pH meter, the four-way valve and the metering pump on each dosing pipeline are electrically connected to the PLC controller through wires.
7. The ammonia stripping cabinet according to any of claims 1-6, wherein the aeration device comprises a blower, a plurality of aeration heads and a plurality of air inlet pipes, an inlet of the blower is communicated with the outside air, the plurality of aeration heads are arranged at the bottom of the accommodating cavity at intervals, and the plurality of air inlet pipes are correspondingly connected to the plurality of aeration heads and are all connected with an outlet of the blower.
8. An ammonia stripping method using the ammonia stripping cabinet as claimed in any one of claims 1 to 7, characterized in that the ammonia stripping method comprises the following steps:
step one, respectively conveying ammonia nitrogen solution and alkali liquor to an accommodating cavity of a cabinet body through a water inlet and a dosing pipeline, and simultaneously starting an aeration device;
and step two, detecting the pH values of the solutions at different positions in the cabinet body, and controlling the dosing pipeline switch and dosing frequency according to the detected pH values.
9. The ammonia stripping method according to claim 8, wherein in the first step, the gas-liquid ratio is controlled to be 800.
10. The ammonia stripping method according to claim 8, wherein the second step is specifically:
when the reading of the first pH meter is less than 11, a metering pump on the first dosing pipeline is opened, the four-way valve correspondingly opens the first dosing pipeline, and the dosing frequency is increased until the reading of the first pH meter is not less than 11;
when the reading of the second pH meter is less than 10, a metering pump on the second dosing pipeline is opened, the four-way valve correspondingly opens the second dosing pipeline, and the dosing frequency is increased until the reading of the second pH meter is not less than 10;
and when the reading of the third pH meter is less than 9, opening a metering pump on the third medicine adding pipeline, correspondingly opening the third medicine adding pipeline by the four-way valve, and increasing the medicine adding frequency until the reading of the third pH meter is between 8.5 and 9.
CN202210970097.3A 2022-08-12 2022-08-12 Ammonia blowing cabinet and ammonia blowing method Active CN115253387B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210970097.3A CN115253387B (en) 2022-08-12 2022-08-12 Ammonia blowing cabinet and ammonia blowing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210970097.3A CN115253387B (en) 2022-08-12 2022-08-12 Ammonia blowing cabinet and ammonia blowing method

Publications (2)

Publication Number Publication Date
CN115253387A true CN115253387A (en) 2022-11-01
CN115253387B CN115253387B (en) 2023-12-08

Family

ID=83751181

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210970097.3A Active CN115253387B (en) 2022-08-12 2022-08-12 Ammonia blowing cabinet and ammonia blowing method

Country Status (1)

Country Link
CN (1) CN115253387B (en)

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0534351A2 (en) * 1991-09-21 1993-03-31 Thyssen Industrie Ag Process and plant for the treatment of highly concentrated ammoniacal waste water
CN1792828A (en) * 2005-11-11 2006-06-28 武汉科梦科技发展有限公司 Process for removing ammonia nitrogen in solution by high dispersing
CN1872707A (en) * 2006-06-15 2006-12-06 武汉理工大学 Removal method and equipment for sucking ammonia nitrogen in waste water through negative pressure of vacuum
CN101774658A (en) * 2010-01-18 2010-07-14 武汉科梦科技发展有限公司 Serial high-dispersion horizontal type ammonia removal equipment
CN102746982A (en) * 2011-04-18 2012-10-24 王淋淋 Multilevel large capacity tank-type photobioreactor capable of inhibiting growth of microalgae on wall
US20140260993A1 (en) * 2013-03-15 2014-09-18 Haven Technology Apparatus and method for gas-liquid separation
CN204039177U (en) * 2014-08-25 2014-12-24 永清环保股份有限公司 A kind of for the treatment of the device containing heavy metal high-concentration ammonia nitrogenous wastewater
CN106861243A (en) * 2017-03-21 2017-06-20 苏州市海崴生物科技有限公司 A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid
CN107596939A (en) * 2017-10-24 2018-01-19 武汉华星光电半导体显示技术有限公司 Detection means, agitator and defoaming method
CN111908545A (en) * 2020-08-11 2020-11-10 江苏蓝晨环保科技有限公司 Multistage stripping system for ammonia nitrogen wastewater
WO2022160563A1 (en) * 2021-01-28 2022-08-04 北京坦思环保科技有限公司 Apparatus and method for deep removal of nitrogen from industrial wastewater by means of anaerobic ammonium oxidation

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0534351A2 (en) * 1991-09-21 1993-03-31 Thyssen Industrie Ag Process and plant for the treatment of highly concentrated ammoniacal waste water
CN1792828A (en) * 2005-11-11 2006-06-28 武汉科梦科技发展有限公司 Process for removing ammonia nitrogen in solution by high dispersing
CN1872707A (en) * 2006-06-15 2006-12-06 武汉理工大学 Removal method and equipment for sucking ammonia nitrogen in waste water through negative pressure of vacuum
CN101774658A (en) * 2010-01-18 2010-07-14 武汉科梦科技发展有限公司 Serial high-dispersion horizontal type ammonia removal equipment
CN102746982A (en) * 2011-04-18 2012-10-24 王淋淋 Multilevel large capacity tank-type photobioreactor capable of inhibiting growth of microalgae on wall
US20140260993A1 (en) * 2013-03-15 2014-09-18 Haven Technology Apparatus and method for gas-liquid separation
CN204039177U (en) * 2014-08-25 2014-12-24 永清环保股份有限公司 A kind of for the treatment of the device containing heavy metal high-concentration ammonia nitrogenous wastewater
CN106861243A (en) * 2017-03-21 2017-06-20 苏州市海崴生物科技有限公司 A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid
CN107596939A (en) * 2017-10-24 2018-01-19 武汉华星光电半导体显示技术有限公司 Detection means, agitator and defoaming method
CN111908545A (en) * 2020-08-11 2020-11-10 江苏蓝晨环保科技有限公司 Multistage stripping system for ammonia nitrogen wastewater
WO2022160563A1 (en) * 2021-01-28 2022-08-04 北京坦思环保科技有限公司 Apparatus and method for deep removal of nitrogen from industrial wastewater by means of anaerobic ammonium oxidation

Also Published As

Publication number Publication date
CN115253387B (en) 2023-12-08

Similar Documents

Publication Publication Date Title
CN201087142Y (en) Solid-liquid separation gas dissolving device
CN104893964B (en) High-solid anaerobic fermentation tank and jet stirring device for same
CN115253387A (en) Ammonia stripping cabinet and ammonia stripping method
CN208667234U (en) Oxygenate apparatus for sewage treatment
KR20000066263A (en) Auto Mixing and Diffusing System of Liquid Chemicals for Water Treatment Plant
CN208378552U (en) A kind of novel low liquid level rotational flow aeration device
CN213286367U (en) Self-suction air type desulfurization solution regeneration tank adopting chemical desulfurization method
CN216584237U (en) Sewage nitrogen and phosphorus removal medicine system
CN1242933C (en) High temperature aerobic digestion device for sludge
CN215783099U (en) Mixed gas centralized preparation gas supply system
KR19990084428A (en) Ozone Sterilization Water Production Equipment
CN205953583U (en) Novel gas pitcher is dissolved in air supporting
KR101157642B1 (en) Apparatus for Dissolving Oxygen Using Bubble
CN108684395A (en) A kind of intelligence microbubble conveying device
KR100301278B1 (en) Automatic fertilizer mixing system
CN206156839U (en) Bed of packings efflux aeration tank
CN110871029A (en) Desulfurization water circulating system
CN200974794Y (en) Seawater desulfurizing deep well aeration device
CN212050678U (en) Sewage disinfection treatment facility
CN215654882U (en) Liquid accelerator adding device
CN213643714U (en) Novel double-tower double-circulation absorption tower for measuring PH value in desulfurization
CN106044982A (en) Novel ozone water hybrid system
CN219242713U (en) Can dismantle venturi fertilizer distributor of being equipped with novel check valve
CN217026497U (en) Retention auxiliary agent adding device
CN205164687U (en) Continuous return circuit gas -liquid reaction unit

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
GR01 Patent grant
GR01 Patent grant