CN205419842U - Circulated online pollutant processing apparatus - Google Patents
Circulated online pollutant processing apparatus Download PDFInfo
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- CN205419842U CN205419842U CN201521025363.7U CN201521025363U CN205419842U CN 205419842 U CN205419842 U CN 205419842U CN 201521025363 U CN201521025363 U CN 201521025363U CN 205419842 U CN205419842 U CN 205419842U
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- moving bed
- desorption
- adsorption system
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Abstract
The utility model relates to a circulated online pollutant processing apparatus, including dynamic adsorption system and dynamic desorption system, the dynamic adsorption system from bottom to top in proper order by sewage storage tank, sewage pretreatment device, remove a bed adsorption tower, adsorption system collection device and water quality testing appearance and link to each other, dynamic desorption system from bottom to top in proper order by desorption agent storage tank, remove a bed desorption tower, the collection device of desorption system and desorption agent parameter detection appearance and link to each other, the shell side both ends interface of removal bed adsorption tower advance, export for heating medium to heating or cooling sewage, removal bed adsorption tower and adsorption system collection device between be equipped with the adsorption system peristaltic pump, the hose end of adsorption system peristaltic pump connect the sewage that moves after the bed adsorption tower is handled, another termination adsorption system collector. This device adsorption material can recycle to quality of water after different time quantums of ability control detection or different temperatures, different flow are handled.
Description
Technical field
This utility model relates to a kind of online pollutant handling arrangement capable of circulation, belongs to sewage-treatment plant technical field.
Background technology
In prior art, the equipment of sewage-treatment plant technical field mostly is static adsorption equipment, static adsorption equipment is not easy to regulation, it is suitable only for using in the detection work that some purposes are relatively limited to, and Dynamic gas-mixing and adsorption devices expense is the highest, and volume is the biggest, taken up space the biggest, and the adsorption temp of pollutant adsorbent equipment can not be dynamically regulated according to monitoring result, the reaction rate of adsorption etc., can not dynamically regulate the desorption temperature of desorption apparatus, desorption rate etc., and adsorbent can not dynamic circulation use, it is unfavorable for the laboratory research of colleges and universities and institute, lack the dynamic adjustable circulating sewage processing system being exclusively used in experimentation.
Utility model content
The purpose of this utility model is to provide a kind of online pollutant handling arrangement capable of circulation, pollutant adsorbs detection online, meets the laboratory research needs of colleges and universities and institute.
For solving above-mentioned technical problem, the technical scheme that this utility model provides is:
A kind of online pollutant handling arrangement capable of circulation, including dynamic adsorption system and dynamic desorption system；Described dynamic adsorption system is connected with water quality testing meter by sewage storage tank, sewage pre-treatment device, moving bed adsorption tower, adsorption system collection device the most successively；Described dynamic desorption system is connected with desorbing agent parameter detecting instrument by desorbing agent storage tank, moving bed desorption column, desorption system collection device the most successively；Shell side two end interface of described moving bed adsorption tower is heat-carrying agent import and export, in order to sewage is heated or cooled；Being provided with adsorption system peristaltic pump between described moving bed adsorption tower and adsorption system collection device, the flexible pipe one of described adsorption system peristaltic pump terminates the sewage after moving bed adsorption tower processes, and another terminates adsorption system catcher.
Saturated adsorption material batch can, saturated adsorption material batch can is had to deposit the adsorbing material reaching adsorption equilibrium accomplished continuously or intermittently discharged connecting at the bottom of described moving bed adsorption tower tower；Described saturated adsorption material batch can import is connected at the bottom of moving bed adsorption tower tower, and outlet is connected with moving bed desorption column tower top；Connecting the regenerative adsorption material having regenerative adsorption material tank, adsorption material batch can to deposit after discharging desorption at the bottom of described moving bed desorption column tower, described regenerative adsorption material tank import is connected at the bottom of moving bed desorption column tower, and outlet is connected to moving bed adsorption tower.
It is provided with effusion meter between described desorbing agent storage tank, moving bed desorption column.
Described adsorption system collection device is several, respectively by hose connection adsorption system peristaltic pump, and different adsorption system collection devices sewage after connecing different time sections or different temperatures, different flow process.
Described adsorption system peristaltic pump is respectively equipped with valve on the connecting line of different adsorption system collection devices, is provided with valve setpoint device on adsorption system peristaltic pump.
Described sewage pre-treatment device is liquid distributing device or centrifugal separating device.
Described desorbing agent parameter detecting instrument is pH analyzer or conductivity measuring instrument.
Described desorbing agent parameter detecting instrument is metal ion detection instrument.
Beneficial effect:
Online pollutant handling arrangement capable of circulation of the present utility model includes dynamic adsorption system and dynamic desorption system, and adsorbing material can recycle.
This device utilizes the sewage after the flexible pipe collection process of peristaltic pump, sewage after process is collected in different automatic collectors respectively, so that water quality testing meter detects the water quality after different time sections or different temperatures, different flow process, and judge to adsorb whether be in adsorption equilibrium state, absorption once enters poised state, experiment can interrupt the water quality of the water processed with guarantee, and save experimental period and add catalyst carrier consumption etc..
Accompanying drawing explanation
Fig. 1: the structural representation of online pollutant handling arrangement capable of circulation of the present utility model.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described in further detail.
A kind of online pollutant handling arrangement capable of circulation, including dynamic adsorption system and dynamic desorption system；Described dynamic adsorption system is connected with water quality testing meter by sewage storage tank, sewage pre-treatment device, moving bed adsorption tower, adsorption system collection device the most successively；Described dynamic desorption system is connected with desorbing agent parameter detecting instrument by desorbing agent storage tank, moving bed desorption column, desorption system collection device the most successively；Shell side two end interface of described moving bed adsorption tower is heat-carrying agent import and export, in order to sewage is heated or cooled；Being provided with adsorption system peristaltic pump between described moving bed adsorption tower and adsorption system collection device, the flexible pipe one of described adsorption system peristaltic pump terminates the sewage after moving bed adsorption tower processes, and another terminates adsorption system catcher.
Connecting saturated adsorption material batch can at the bottom of described moving bed adsorption tower tower, saturated adsorption material batch can deposits the adsorbing material reaching adsorption equilibrium accomplished continuously or intermittently discharged；Described saturated adsorption material batch can import is connected at the bottom of moving bed adsorption tower tower, and outlet is connected with moving bed desorption column tower top；Connecting the regenerative adsorption material having regenerative adsorption material tank, adsorption material batch can to deposit after discharging desorption at the bottom of described moving bed desorption column tower, described regenerative adsorption material tank import is connected at the bottom of moving bed desorption column tower, and outlet is connected to moving bed adsorption tower.
It is provided with effusion meter between described desorbing agent storage tank, moving bed desorption column.Described adsorption system collection device is several, respectively by hose connection adsorption system peristaltic pump, and different adsorption system collection devices sewage after connecing different time sections or different temperatures, different flow process.Described adsorption system peristaltic pump is respectively equipped with valve on the connecting line of different adsorption system collection devices, is provided with valve setpoint device on adsorption system peristaltic pump.Described sewage pre-treatment device is liquid distributing device or centrifugal separating device.Described desorbing agent parameter detecting instrument is pH analyzer or conductivity measuring instrument.Described desorbing agent parameter detecting instrument is metal ion detection instrument.
The above; it it is only preferred embodiment of the present utility model; not this utility model is made any pro forma restriction; any those skilled in the art; in the range of without departing from technical solutions of the utility model; according to technical spirit of the present utility model, any simple amendment being made above example, equivalent and improvement etc., within all still falling within the protection domain of technical solutions of the utility model.
Claims (8)
1. an online pollutant handling arrangement capable of circulation, it is characterised in that: include dynamic adsorption system and dynamic desorption system；Described dynamic adsorption system is connected with water quality testing meter by sewage storage tank, sewage pre-treatment device, moving bed adsorption tower, adsorption system collection device the most successively；Described dynamic desorption system is connected with desorbing agent parameter detecting instrument by desorbing agent storage tank, moving bed desorption column, desorption system collection device the most successively；Shell side two end interface of described moving bed adsorption tower is heat-carrying agent import and export, in order to sewage is heated or cooled；Being provided with adsorption system peristaltic pump between described moving bed adsorption tower and adsorption system collection device, the flexible pipe one of described adsorption system peristaltic pump terminates the sewage after moving bed adsorption tower processes, and another terminates adsorption system catcher.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 1, it is characterised in that: there are saturated adsorption material batch can, saturated adsorption material batch can to deposit the adsorbing material reaching adsorption equilibrium accomplished continuously or intermittently discharged connecting at the bottom of described moving bed adsorption tower tower；Described saturated adsorption material batch can import is connected at the bottom of moving bed adsorption tower tower, and outlet is connected with moving bed desorption column tower top；Connecting the regenerative adsorption material having regenerative adsorption material tank, adsorption material batch can to deposit after discharging desorption at the bottom of described moving bed desorption column tower, described regenerative adsorption material tank import is connected at the bottom of moving bed desorption column tower, and outlet is connected to moving bed adsorption tower.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 1, it is characterised in that: between described desorbing agent storage tank, moving bed desorption column, it is provided with effusion meter.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 1, it is characterized in that: described adsorption system collection device is several, respectively by hose connection adsorption system peristaltic pump, different adsorption system collection devices sewage after connecing different time sections or different temperatures, different flow process.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 4, it is characterised in that: described adsorption system peristaltic pump is respectively equipped with valve on the connecting line of different adsorption system collection devices, is provided with valve setpoint device on adsorption system peristaltic pump.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 1, it is characterised in that: described sewage pre-treatment device is liquid distributing device or centrifugal separating device.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 1, it is characterised in that: described desorbing agent parameter detecting instrument is pH analyzer or conductivity measuring instrument.
Online pollutant handling arrangement capable of circulation the most as claimed in claim 1, it is characterised in that: described desorbing agent parameter detecting instrument is metal ion detection instrument.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521025363.7U CN205419842U (en) | 2015-12-11 | 2015-12-11 | Circulated online pollutant processing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521025363.7U CN205419842U (en) | 2015-12-11 | 2015-12-11 | Circulated online pollutant processing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205419842U true CN205419842U (en) | 2016-08-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521025363.7U Expired - Fee Related CN205419842U (en) | 2015-12-11 | 2015-12-11 | Circulated online pollutant processing apparatus |
Country Status (1)
| Country | Link |
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| CN (1) | CN205419842U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115583688A (en) * | 2022-01-19 | 2023-01-10 | 河南理工大学 | Spiral fluidization continuous adsorption device and method based on coal gangue-based molecular sieve |
-
2015
- 2015-12-11 CN CN201521025363.7U patent/CN205419842U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115583688A (en) * | 2022-01-19 | 2023-01-10 | 河南理工大学 | Spiral fluidization continuous adsorption device and method based on coal gangue-based molecular sieve |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160803 Termination date: 20181211 |
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| CF01 | Termination of patent right due to non-payment of annual fee |