CN2650844Y - Automatic acid supplier of ceramic filter - Google Patents
Automatic acid supplier of ceramic filter Download PDFInfo
- Publication number
- CN2650844Y CN2650844Y CN 200320124571 CN200320124571U CN2650844Y CN 2650844 Y CN2650844 Y CN 2650844Y CN 200320124571 CN200320124571 CN 200320124571 CN 200320124571 U CN200320124571 U CN 200320124571U CN 2650844 Y CN2650844 Y CN 2650844Y
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- CN
- China
- Prior art keywords
- acid
- ball valve
- control system
- pneumatic ball
- flushing pipeline
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- Expired - Fee Related
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Abstract
An automatic acid proportioning apparatus for ceramic filter is provided, which comprises an acid proportioning part, an acid feeding part, and a control system, wherein, a pneumatic ball valve for feeding acid, a pneumatic ball valve for feeding water, a liquid level meter, and a metering pump are arranged on the top of a sealed stainless steel cylinder; a pressure transmitter (sensor) is mounted in the back flushing pipeline; above (the) devices are connected to the control system; the acid outlet of the metering pump is open to the back flushing pipeline; under instruction of the control system, the ball valve for feeding acid and the ball valve for feeding water ware (are) opened to mix (proportion) acid automatically, and, with the pressure transmitter, supply acid automatically (under the function of the pressure transmitter, the acid is automatically supplied)to clean the filter plate. The apparatus can mix acid at an accurate concentration, delivers (the apparatus has) good cleaning effect, and is safe and reliable, and reduces labor intensity of manual acid proportioning.
Description
Technical field
The utility model relates to the complex acid device on a kind of solid-liquid separating equipment, specifically the automatic mixing acid device of ceramic filter.
Background technology
Ceramic filter is a kind of solid-liquid separating equipment, in the equipment course of work, its filter medium filter plate will pass through suction strainer, drains, discharging, four continuous courses of work of backwash, moves in circles, and finished the cyclic process of above-mentioned four actions by distributing valve control rotor in a revolution.
Some circle ceramic filtering plates are housed as filter medium on the main shaft of ceramic filter, each circle is equipped with 12 filter plates, main shaft drive filter plate rotates in the feed chute of going forward side by side when work, the material that needs dehydration is housed in the hopper, and filter plate has passed through filter cake formation, cake dewatering, has peeled off and washed four-stage in a revolution.When dehydration, the water in the material is discharged after the filter plate micropore enters inside from the filter plate outside.When flushing, water outwards oozes out by micropore from filter plate inside, so the stage can be described as backwash again.After filter cake on filter plate was stripped from, the filter plate surface still had remaining material, and the micropore on the part filter plate has blocked situation, adopts the method for backwash like this, just can remove surface residues material and mediation micropore.
Glassware for drinking water during backwash has certain pressure, form the press water of 0.06Mpa to 0.08Mpa by filtration, decompression and constant-voltage system, enter the filter plate inner chamber by pipeline, distributing valve, under differential pressure action, outwards flow through the filter plate micropore, wash out material residual on the filter plate and mediation filter plate micropore, thereby reach the purpose of cleaning and ensureing filter efficiency.
In the job applications of reality, particularly after ceramic filter moves a period of time, often contained some become branch's fouling on filter plate in the material, stopped up the filter plate micropore, even backwash is arranged, also can't remove, so that the stopping state of ceramic filter can aggravate along with the lengthening of service time, therefore must regularly handle the fouling tendency material to these fouling tendency materials.
Summary of the invention
In order to overcome the scale formation of filter plate micropore, the utility model provides a kind of automatic mixing acid device of wash water, it is controlled automatically by microsystem, make the proportioning of acid, water in the mixed process realize control automatically, mixed acid solution is provided in the counter-flushing pipeline by certain flow automatically, mix once more with water in the counter-flushing pipeline according to the hydraulic pressure situation, finally reach the fouling tendency material in the dissolving filter plate micropore, the purpose of mediation filter plate micropore.
By its technical scheme of automatic mixing acid device that the utility model proposes be: on the position line at round center is crossed at the stainless steel drum top of a sealing, lead to and be furnished with into concentrated acid pneumatic ball valve and flanged fitting, water inlet pneumatic ball valve and flanged fitting, liquid level gauge, measuring pump in the bucket successively, wherein advancing concentrated acid pneumatic ball valve and flanged fitting is connected with the concentrated acid bucket by the concentrated acid pipe, water inlet pneumatic ball valve and flanged fitting are connected with running water pipe, the entrance point of measuring pump gos deep in the bucket, and its outlet is connected with counter-flushing pipeline.In addition, advancing sour ball valve, water intake ball valve, liquid level gauge and measuring pump all has circuit to link to each other with the Control System of Microcomputer of this device.
The utility model is made up of complex acid part, confession acid moieties and control system, complex acid part mainly by the stainless steel drum, advance concentrated acid pneumatic ball valve and flanged fitting, water inlet pneumatic ball valve and flanged fitting, liquid level is taken into account associated pipe and is constituted, and links to each other with control system.By giving the predefined value of control system, reach the quantitative control of into acid and water inlet, in drum, to obtain the diluted acid of certain proportioning.
The acid moieties that supplies of the present utility model mainly is made of pressure sensor in measuring pump, the counter-flushing pipeline and associated pipe, measuring pump has circuit to link to each other with control system with pressure sensor, when the pressure in the counter-flushing pipeline reached predefined force value, control system started measuring pump and supplies acid work.
Control system of the present utility model is made up of microcomputer and other electronic devices and components, is known technology.
Use this device, have the following advantages:
1, complex acid concentration is accurate, and its concentration can suitably be adjusted at any time, has stopped the instability and the fault phenomenon of artificial complex acid.
2, cleaning performance is good, cooperates other cleaning ways can thoroughly dredge the filter plate micropore, in time recovers the filter plate serviceability.
3, safe and reliable, stop potential safety hazard, reduced the labour intensity of artificial complex acid.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure 1, stainless steel cask, 2, measuring pump, 3, liquid level gauge, 4, pressure sensor, 5, flanged fitting, 6, the water inlet pneumatic ball valve, 7, advance the concentrated acid pneumatic ball valve, 8, the concentrated acid pipe, 9, running water pipe, 10, backwash tube, 11, control system
Specific implementation method
Embodiment is explained in detail the utility model below in conjunction with accompanying drawing.
As shown in Figure 1, top at a stainless steel drum (1) that seals, concentrated acid pneumatic ball valve (7) and flanged fitting (5), water inlet pneumatic ball valve (6) and flanged fitting (5), liquid level gauge (3) and measuring pump (2) have been set gradually on the linear position by the center of circle, its mouth of pipe or pipe all stretch in the bucket, the flange part that advances sour ball valve is connected with concentrated acid pipe (8), the flange part of water intake ball valve is connected with running water pipe (9), and above-mentioned device all has circuit to lead to the control system (11) of this device; The acid inlet of measuring pump (2) is connected with one section tetrafluoro flexible pipe, and its length touches stainless steel drum (1) bottom substantially, and the acid mouth that goes out of measuring pump is connected with one section tetrafluoro flexible pipe equally, and its other end is connected with counter-flushing pipeline (10); In counter-flushing pipeline (10), a pressure sensor (4) is housed, there is line to lead to control system (11) on it; Stainless steel drum size is φ 700 * 800mm in the present embodiment.
The utility model is work like this: when complex acid partly moves, advancing the moving ball valve of acid gas opens, concentrated acid enters in the drum through valve, flange, when the liquid level of concentrated acid in drum reaches predefined value, liquid level gauge is given signal of control system, this moment, control system was closed into sour ball valve, and open into water pneumatic ball valve immediately, water mixes with acid in ball valve, flange enter bucket, when liquid level reaches predefined value, during the dilute acid soln concentration ratio promptly set, liquid level gauge is given signal of control system, and control system is closed water intake ball valve.Treat water with after acid fully mixes, can obtain the diluted acid of our desired concn.
During for the acid moieties operation, when the water pressure in the counter-flushing pipeline reaches predefined force value, pressure sensor can be given signal of control system, control system control measuring pump starts, the diluted acid for preparing in the bucket is pumped in the counter-flushing pipeline, enter filter plate inside with the backwash current, acid solution is dissolved scale forming matter, reach the cleaning purpose.Certain hydraulic pressure can prevent diluted acid in counter-flushing pipeline, reflux pour in down a chimney, corrosion device.When stopping backwashing procedures, control system is promptly closed measuring pump, and diluted acid promptly stops pumping.
Claims (2)
1, the automatic mixing acid device of ceramic filter, it is by the complex acid part, form for acid moieties and control system, it is characterized in that on the position line at round center is crossed at the stainless steel drum top of a sealing, leading to and be furnished with into concentrated acid pneumatic ball valve and flanged fitting in the bucket successively, water inlet pneumatic ball valve and flanged fitting, liquid level gauge, measuring pump, wherein advancing concentrated acid pneumatic ball valve and flanged fitting is connected with the concentrated acid bucket by the concentrated acid pipe, water inlet pneumatic ball valve and flanged fitting are connected with running water pipe, the entrance point of measuring pump gos deep in the drum, its outlet is connected with counter-flushing pipeline, advances sour ball valve, water intake ball valve, liquid level gauge all has circuit to link to each other with the control system of this device with measuring pump.
2, by the automatic mixing acid device of the described ceramic filter of claim 1, it is characterized in that in counter-flushing pipeline, a pressure sensor is housed, have line to lead to control system on it.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320124571 CN2650844Y (en) | 2003-11-13 | 2003-11-13 | Automatic acid supplier of ceramic filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320124571 CN2650844Y (en) | 2003-11-13 | 2003-11-13 | Automatic acid supplier of ceramic filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2650844Y true CN2650844Y (en) | 2004-10-27 |
Family
ID=34349044
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200320124571 Expired - Fee Related CN2650844Y (en) | 2003-11-13 | 2003-11-13 | Automatic acid supplier of ceramic filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2650844Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1978028B (en) * | 2005-12-09 | 2010-09-08 | 安徽铜都特种环保设备股份有限公司 | On-line circulated washing method of ceramic filter |
| CN102240472A (en) * | 2011-05-17 | 2011-11-16 | 云南大红山管道有限公司 | Ceramic plate pickling device |
| CN103657233A (en) * | 2013-12-06 | 2014-03-26 | 贵州开磷（集团）有限责任公司 | Ceramic filter cleaning system |
| CN104084294A (en) * | 2014-07-04 | 2014-10-08 | 云南大红山管道有限公司 | Ceramic filtering machine tank |
| CN107262429A (en) * | 2017-06-26 | 2017-10-20 | 华电电力科学研究院 | A kind of disk dewatering machine on-line cleaning device |
| CN107961580A (en) * | 2017-12-01 | 2018-04-27 | 核工业烟台同兴实业集团有限公司 | A kind of ceramic filter pickling cyclic utilization system |
-
2003
- 2003-11-13 CN CN 200320124571 patent/CN2650844Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1978028B (en) * | 2005-12-09 | 2010-09-08 | 安徽铜都特种环保设备股份有限公司 | On-line circulated washing method of ceramic filter |
| CN102240472A (en) * | 2011-05-17 | 2011-11-16 | 云南大红山管道有限公司 | Ceramic plate pickling device |
| CN103657233A (en) * | 2013-12-06 | 2014-03-26 | 贵州开磷（集团）有限责任公司 | Ceramic filter cleaning system |
| CN104084294A (en) * | 2014-07-04 | 2014-10-08 | 云南大红山管道有限公司 | Ceramic filtering machine tank |
| CN107262429A (en) * | 2017-06-26 | 2017-10-20 | 华电电力科学研究院 | A kind of disk dewatering machine on-line cleaning device |
| CN107961580A (en) * | 2017-12-01 | 2018-04-27 | 核工业烟台同兴实业集团有限公司 | A kind of ceramic filter pickling cyclic utilization system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |