CN204044582U - PH value circulation supervisory system - Google Patents
PH value circulation supervisory system Download PDFInfo
- Publication number
- CN204044582U CN204044582U CN201420443204.8U CN201420443204U CN204044582U CN 204044582 U CN204044582 U CN 204044582U CN 201420443204 U CN201420443204 U CN 201420443204U CN 204044582 U CN204044582 U CN 204044582U
- Authority
- CN
- China
- Prior art keywords
- flow cell
- absorption tower
- meter
- supervisory system
- valve
- 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
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of pH value circulation supervisory system, comprise absorption tower and ebullator, absorption tower is connected with ebullator formation major loop, described circulating-pump outlet is provided with circulation branch road, described circulation branch road is provided with flow cell, and described flow cell water inlet pipe is provided with operation valve, and described flow cell top is provided with pH meter, described pH meter is fixedly connected with flow cell, and flow cell rising pipe is connected with absorption tower.The utility model is when pH meter needs to safeguard or change, and closed control valve, discharges the circulation fluid of flow cell inside, just can safeguard or change pH meter, so both can safeguard or change pH meter, not affecting again the normal operation on absorption tower.
Description
Technical field
The utility model relates to chemical emission process field, and in particular, the utility model relates to a kind of pH value circulation supervisory system.
Background technology
At present, in waste gas treatment process, adopt liquid absorption process comparatively common, such as carry out packed tower or rotating stream tray scrubber inverse spray circulation fluid to acid waste gas to absorb, and generally the pH value of absorbing liquid needs to control, otherwise be difficult to the effect that ensures to absorb and stability, the detection of pH value needs to be completed by pH meter, thus the installation site of pH meter is particularly important, as install unfortunately when, the problem such as inaccurate detected may be caused.Conventional bottom pH meter being all arranged on to spray column, i.e. the liquid level region of circulation groove.This mounting means may bring many-sided problem in actual use, when pH meter needs to safeguard or change, circulation groove liquid level must be put to pH meter height, because the uncertainty of operation, so cause waste and the time waste of circulation fluid, special in tower diameter is larger, discharge cycle liquid needs for a long time.Meanwhile, because tower body is comparatively large, the mixing of circulation tank liquor is changed not in time, and cause pH value to occur delayed, system is matched add alkali or add acid function can not be implemented in time, have impact on the absorptive character of circulation fluid.
Utility model content
The purpose of this utility model is to solve existing above-mentioned problem, provides a kind of pH value circulation supervisory system.
For realizing above object, the technical solution of the utility model is a kind of pH value circulation supervisory system, comprise absorption tower and ebullator, absorption tower is connected with ebullator formation major loop, it is characterized in that, described circulating-pump outlet is provided with circulation branch road, described circulation branch road is provided with flow cell, and described flow cell water inlet pipe is provided with operation valve, and described flow cell top is provided with pH meter, described pH meter is fixedly connected with flow cell, and flow cell rising pipe is connected with absorption tower.The operation valve on circulation branch road is utilized to regulate the circulating fluid flow rate flowing into flow cell, the circulation fluid flowing into flow cell measures the pH value of circulation fluid by pH meter, the circulation fluid of flow cell flows back to absorption tower by flow cell rising pipe, when pH meter needs to safeguard or change, closed control valve, discharges the circulation fluid of flow cell inside, just can safeguard or change pH meter, so both can safeguard or change pH meter, not affecting again the normal operation on absorption tower.
As preferably, described flow cell bottom is provided with blow-off pipe, and described blow-off pipe is fixedly connected with flow cell, and described blow-off pipe is provided with blowoff valve.When needing blowdown, open blowoff valve, by blow-off pipe, the sewage in flow cell is discharged.
As preferably, described flow cell rising pipe is provided with valve, and described valve is fixedly connected with flow cell rising pipe.When safeguarding or change pH meter, the valve on flow cell rising pipe refluxes for preventing the circulation fluid of inside, absorption tower.
As preferably, described flow cell bottom is funnel-form.Flow cell lower hopper shape, facilitates sewage to discharge.
As preferably, described inside, absorption tower is provided with spraying layer, and described spraying layer is connected with major loop water inlet pipe, is provided with processing layer below described spraying layer, and described processing layer is fixedly connected with absorption tower.The circulation fluid of major loop sprays processing layer by spraying layer, and circulation fluid processes by processing layer, finally flows back to bottom absorption tower.
As preferably, the major loop of described circulating-pump outlet is provided with variable valve, and described variable valve is fixedly connected with major loop.Variable valve on major loop can regulate circulating fluid flow rate, regulates like this according to need of production.
As preferably, described absorption tower side is provided with exhaust gas inlet pipe, and described exhaust gas inlet pipe is fixedly connected with absorption tower.Such convenience carries out maintenance and repair to absorption tower.
The utility model has following beneficial effect: when pH meter needs to safeguard or change, closed control valve, discharges the circulation fluid of flow cell inside, just can safeguard or change pH meter, so both can safeguard or change pH meter, not affecting again the normal operation on absorption tower.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the present utility model.
1, ebullator, 11, variable valve, 12, major loop, 2, absorption tower, 21, spraying layer, 22, processing layer, 23, exhaust gas inlet pipe, 3, flow cell, 31, operation valve, 32, flow cell water inlet pipe, 33, valve, 34, flow cell rising pipe, 35, blowoff valve, 36, blow-off pipe, 37, pH meter.
Embodiment
Below in conjunction with specific embodiment, and by reference to the accompanying drawings, the technical solution of the utility model is further described:
Embodiment: pH value circulation supervisory system (see accompanying drawing 1), comprise absorption tower 2 and ebullator 1, absorption tower 2 is connected with ebullator 1 and forms major loop 12, described ebullator 1 outlet is provided with circulation branch road, described circulation branch road is provided with flow cell 3, described flow cell water inlet pipe 32 is provided with operation valve 31, described flow cell 3 top is provided with pH meter 37, described pH meter 37 is fixedly connected with flow cell 3, flow cell rising pipe 34 is connected with absorption tower 2, described flow cell 3 bottom is provided with blow-off pipe 36, described blow-off pipe 36 is fixedly connected with flow cell 3, described blow-off pipe 36 is provided with blowoff valve 35, described flow cell rising pipe 34 is provided with valve 33, described valve 33 is fixedly connected with flow cell rising pipe 34, described flow cell 3 bottom is funnel-form, described inside, absorption tower 2 is provided with spraying layer 21, described spraying layer 21 is connected with major loop 12 water inlet pipe, processing layer 22 is provided with below described spraying layer 21, described processing layer 22 is fixedly connected with absorption tower 2, the major loop 12 that described ebullator 1 exports is provided with variable valve 11, described variable valve 11 is fixedly connected with major loop 12, described absorption tower 2 side is provided with exhaust gas inlet pipe 23, described exhaust gas inlet pipe 23 is fixedly connected with absorption tower 2.
During operation, ebullator 1 starts, absorption tower Inner eycle liquid is delivered to spraying layer and flow cell by described ebullator, control valve and operation valve, a small amount of circulation fluid is circulated pond, main circulation fluid enters spraying layer, and then be sprayed on processing layer, to meet the exhaust-gas treatment entered from exhaust gas inlet pipe, can realize again monitoring the pH value of the circulation fluid in absorption tower simultaneously, when pH meter or flow cell need to be serviced, only need closed control valve and valve, or pH meter pulled down or carries out blowdown process by opening valve, so namely do not affect the normal process of absorption tower for waste gas.Conventional maintenance can be realized again.
Above-mentioned embodiment is used for explaining and the utility model is described; instead of the utility model is limited; in the protection domain of spirit of the present utility model and claim, any amendment make the utility model and change, all fall into protection domain of the present utility model.
Claims (7)
1. a pH value circulation supervisory system, comprise absorption tower and ebullator, absorption tower is connected with ebullator formation major loop, it is characterized in that, described circulating-pump outlet is provided with circulation branch road, and described circulation branch road is provided with flow cell, described flow cell water inlet pipe is provided with operation valve, described flow cell top is provided with pH meter, and described pH meter is fixedly connected with flow cell, and flow cell rising pipe is connected with absorption tower.
2. pH value circulation supervisory system according to claim 1, it is characterized in that, described flow cell bottom is provided with blow-off pipe, and described blow-off pipe is fixedly connected with flow cell, and described blow-off pipe is provided with blowoff valve.
3. pH value circulation supervisory system according to claim 2, it is characterized in that, described flow cell rising pipe is provided with valve, and described valve is fixedly connected with flow cell rising pipe.
4. pH value circulation supervisory system according to claim 3, it is characterized in that, described flow cell bottom is funnel-form.
5. pH value circulation supervisory system according to claim 1, it is characterized in that, described inside, absorption tower is provided with spraying layer, and described spraying layer is connected with major loop water inlet pipe, be provided with processing layer below described spraying layer, described processing layer is fixedly connected with absorption tower.
6., according to the pH value circulation supervisory system of claim 1-5 wherein described in any one, it is characterized in that, the major loop of described circulating-pump outlet is provided with variable valve, and described variable valve is fixedly connected with major loop.
7. pH value circulation supervisory system according to claim 6, it is characterized in that, described absorption tower side is provided with exhaust gas inlet pipe, and described exhaust gas inlet pipe is fixedly connected with absorption tower.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420443204.8U CN204044582U (en) | 2014-08-07 | 2014-08-07 | PH value circulation supervisory system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420443204.8U CN204044582U (en) | 2014-08-07 | 2014-08-07 | PH value circulation supervisory system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204044582U true CN204044582U (en) | 2014-12-24 |
Family
ID=52245230
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201420443204.8U Expired - Fee Related CN204044582U (en) | 2014-08-07 | 2014-08-07 | PH value circulation supervisory system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204044582U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111807495A (en) * | 2020-08-05 | 2020-10-23 | 西安热工研究院有限公司 | Water quality control device and method for preventing corrosion of indirect air-cooling circulating water system |
-
2014
- 2014-08-07 CN CN201420443204.8U patent/CN204044582U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111807495A (en) * | 2020-08-05 | 2020-10-23 | 西安热工研究院有限公司 | Water quality control device and method for preventing corrosion of indirect air-cooling circulating water system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104258719B (en) | Desulfuration, denitration and dust removal (PM2.5 removal) three-in-one technical system for boiler exhaust gas by adopting ammonia method | |
CN101816888A (en) | Wet flue gas desulfurization absorption tower for power plant | |
CN101322906A (en) | Intelligent system for processing waste gas | |
CN204582902U (en) | A kind of waste gas absorption spray equipment | |
CN201223766Y (en) | PLC automatic control waste gas treater | |
CN204044582U (en) | PH value circulation supervisory system | |
CN103252157A (en) | Vertical type acid-base waste gas washing tower | |
CN204051315U (en) | A kind of water spray cleaner | |
CN203469796U (en) | Boiler flue gas desulfurization tower | |
CN208799958U (en) | A kind of horizontal calcium method desulfurizing tower | |
CN204543953U (en) | A kind of novel absorbent tower | |
CN205903759U (en) | Automatic formula active carbon adsorption device is prevented blockking up in washing | |
CN109381988A (en) | A kind of device preventing ammonia process desulfuration tower Crystallization Plugging | |
CN204051384U (en) | A kind of ammonia washing recovering device | |
CN204395709U (en) | A kind of wet dust removal filter | |
CN209501312U (en) | A kind of device preventing ammonia process desulfuration tower Crystallization Plugging | |
CN208943788U (en) | A kind of Ammonia recovery processing system | |
CN102631819A (en) | Tail gas washing method for reducing ammonia consumption | |
CN207667431U (en) | Integral type sprays recycle unit in demisting deodorization and shower water | |
CN207591603U (en) | A kind of SNCR denitration device | |
CN104492240A (en) | Waste gas purification device | |
CN205730842U (en) | Waste water sub-prime collection and treatment device | |
CN205700093U (en) | A kind of sodium pyrosulfite produces form waste gas of sulfur dioxide and utilizes device | |
CN219023835U (en) | Ammonia recovery system based on ammonia preparation | |
CN209230939U (en) | A kind of ammonia process of desulfurization nozzle performance comprehensive detection device |
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: 20141224 Termination date: 20200807 |
|
CF01 | Termination of patent right due to non-payment of annual fee |