CN108620241A - Full-automatic fluid slagging-off seperator and its control method - Google Patents
Full-automatic fluid slagging-off seperator and its control method Download PDFInfo
- Publication number
- CN108620241A CN108620241A CN201810263615.1A CN201810263615A CN108620241A CN 108620241 A CN108620241 A CN 108620241A CN 201810263615 A CN201810263615 A CN 201810263615A CN 108620241 A CN108620241 A CN 108620241A
- Authority
- CN
- China
- Prior art keywords
- plc
- fluid
- centrifugal chamber
- chamber casing
- frequency converter
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B13/00—Control arrangements specially designed for centrifuges; Programme control of centrifuges
Abstract
The invention discloses full-automatic fluid slagging-off seperator and its control methods, it includes pedestal (1), shell (2), main motor (3), auxiliary motor (4), centrifugal chamber casing (5), clinker collecting box(13)And removing device, cylindrical fluid nozzle is provided in centrifugal chamber casing(6)It is exported with fluid(7), cylindrical fluid nozzle passes through pump(8)It is in communication with the outside, signal is connected with PLC on main motor(14)With the first frequency converter(15), the centrifugal chamber casing is built-in with the strength of fluid sensor being connect with PLC signals(17), pressure sensor is connected on pump(16), pressure sensor signal is connected with the second frequency converter(18), the second frequency converter connect with PLC signals, and clinker collecting box is built-in with the weighing sensor being connect with PLC signals(19).The beneficial effects of the invention are as follows stable, reliable, reducing human cost simultaneously reduces the consumption of the unnecessary operation in daily production.
Description
Technical field
The present invention relates to iundustrial oil, the slagging-off processing equipment of liquid more particularly to fluid slagging-off seperator and its controlling parties
Method.
Background technology
Oil, liquid mainly play a part of lubrication, cooling, flushing device pipeline, are using process in modern industrial production
In have small mechanical admixture and incorporate in oil, liquid, after the mechanical admixture in oil, liquid reaches certain amount, inevitably
The product quality processed is damaged.Therefore oil, liquid at this moment cannot use, it is necessary to oil, the liquid more renewed, containing big
If the oil of amount mechanical admixture, liquid direct emission will produce pollution, needed using large size processing if carrying out secondary recovery processing
Equipment, processing cost is high, and the period is long.
Chinese invention patent publication number CN105195336A discloses fluid and automatically removes the gred seperator thus, it includes base
Seat (1), shell (2), main motor (3), auxiliary motor (4), centrifugal chamber casing (5) and removing device, centrifugal chamber casing, shell, main motor
It is fixed on pedestal with auxiliary motor, centrifugal chamber casing fits in be sequentially connected in shell and respectively with main motor and auxiliary motor, centrifugation
Cylindrical fluid nozzle (6) and fluid outlet (7) are provided in cavity, the height of fluid outlet is higher than cylindrical fluid nozzle,
Cylindrical fluid nozzle is in communication with the outside by pump (8), and cylindrical fluid nozzle surface is evenly equipped with several spray orifices, removing device position
Include the scraper (9) close to centrifugal chamber casing inner wall inside centrifugal chamber casing.The patent can be completed online to containing a large amount of machineries
The filtering of the oil, liquid of impurity, forms automatic continuous cyclic process, ensure that oil, liquid normal operating conditions, reduce oil,
The discharge of liquid and treating capacity.But fluid slagging-off seperator still needs in filtering, the procedure connection for being dehydrated, striking off, cleaning
Manual operation switches, and the working environment of fluid slag remover is more dangerous, needs one kind being capable of each work of real fully automatic operation
The fluid slagging-off seperator of sequence.
Invention content
The technical problem to be solved by the present invention is to existing fluid slagging-off seperators to need in the linking switching of each process
Manual intervention is wanted, hidden danger is brought to personal safety, increases production cost, a kind of full-automatic fluid slagging-off separation is provided thus
Machine and its control method.
The technical scheme is that:Full-automatic fluid slagging-off seperator, it includes pedestal, shell, main motor, auxiliary electricity
Machine, centrifugal chamber casing, clinker collecting box and removing device are provided with cylindrical fluid nozzle and fluid outlet, circle in centrifugal chamber casing
Cylindricality fluid nozzle is in communication with the outside by pump, and signal is connected with PLC and the first frequency converter on the main motor, on the PLC
Signal is connected with strength of fluid sensor, and pressure sensor is connected on the pump, and the pressure sensor signal is connected with
Two frequency converters, second frequency converter are connect with PLC signals, and the clinker collecting box is built-in with weighs with what PLC signals were connect
Sensor.
Clinker collecting box described in said program at least there are two, be located on the conveyer belt that is connect with PLC signals.
The control method of full-automatic fluid slagging-off seperator, it includes the following steps:(1), filtering control:Filtering control:
After fluid concentration is more than setting maximum concentration, system starts, and PLC drives main motor to start, centrifugal chamber casing rotation, PLC drivings
Fluid is pumped by cylindrical fluid nozzle in centrifugal chamber casing by pump startup, the input oil liquid pressure of pressure sensor detection pump,
So that the input hydraulic pressure of pump is 0.3MPa;(2), dehydration control:PLC control pumps shut down, and the first frequency converter is controlled by PLC
Rotating speed be 3080 RPM-3120 RPM;(3), cleaning control:PLC transfer tubes after fluid concentration reaches setting minimum concentration
It starts to work, new oil, liquid is driven into centrifugal chamber casing, remove the internal remaining sludge not peeled off.
Another control method of full-automatic fluid slagging-off seperator, it includes the following steps:(1), filtering control:Filtering
Control:After fluid concentration is more than setting maximum concentration, system starts, and PLC drives main motor to start, centrifugal chamber casing rotation, PLC
Fluid is pumped by cylindrical fluid nozzle in centrifugal chamber casing by driving pump startup, the input fluid pressure of pressure sensor detection pump
Power so that the input hydraulic pressure of pump is 0.3MPa;(2), dehydration control:PLC control pumps shut down, and are become by PLC controls first
The rotating speed of frequency device is 3080 RPM-3120 RPM;(3), strike off control:Weighing sensor weighed to clinker collecting box and with
Preset desired value compares in PLC, and PLC controls conveyer belt and is delivered to the clinker collecting box equipped with sludge after more than desired value
Other stations, unloaded clinker collecting box are delivered to below centrifugal chamber casing;(4), cleaning control:When fluid concentration reaches setting most
PLC transfer tubes are started to work after low concentration, and new oil, liquid are driven into centrifugal chamber casing, remove what internal residue was not peeled off
Sludge.
The beneficial effects of the invention are as follows by using PLC and frequency converter as the automation control of core, being equipped with multiple sensors
The state of each component is detected, and monitors in real time and manages in conjunction with man-machine interface, the complex control of traditional circuit has been reformed, has reduced system
System operability simultaneously improves system function, and equipment is made to have higher stability and reliability, and solving centrifugal separator can not entirely certainly
The problem of dynamic operation.
Description of the drawings
Fig. 1 is schematic structural view of the invention;
In figure, 1, pedestal, 2, shell, 3, main motor, 4, auxiliary motor, 5, centrifugal chamber casing, 6, cylindrical fluid nozzle, 7, fluid goes out
Mouthful, 8, pump, 9, scraper, 10, air-leg, 11, gas source nozzle, 12, baffle, 13, clinker collecting box, 14, PLC, the 15, first frequency conversion
Device, 16, pressure sensor, 17, strength of fluid sensor, the 18, second frequency converter, 19, weighing sensor.
Specific implementation mode
The seperator as shown in Figure 1, the full-automatic fluid of the present invention removes the gred, it includes pedestal 1, shell 2, main motor 3, auxiliary electricity
Machine 4, centrifugal chamber casing 5, clinker collecting box 13 and removing device are provided with cylindrical fluid nozzle 6 in centrifugal chamber casing and fluid go out
Mouth 7, cylindrical fluid nozzle are in communication with the outside by pump 8, and signal is connected with PLC15 and the first frequency converter on the main motor
Signal is connected with strength of fluid sensor 17 on 15, the PLC, and pressure sensor 16 is connected on the pump, and the pressure passes
Sensor signal is connected with the second frequency converter 18, and second frequency converter is connect with PLC signals, the clinker collecting box be built-in with
The weighing sensor 19 of PLC signals connection.
The full-automatic fluid slagging-off seperator of the present invention is disclosed with Chinese invention patent publication number CN105195336A substantially
The fluid seperator that automatically removes the gred it is identical, the baffle 12 able to turn on or off driven by air-leg is fitted in centrifugal chamber casing bottom,
The open top of clinker collecting box simultaneously faces baffle, to receive the sludge being discharged in centrifugal chamber casing.Difference lies in more PLC,
One frequency converter, the second frequency converter, weighing sensor, pressure sensor and strength of fluid sensor, and rely on above-mentioned component control
The method of liquefaction liquid slagging-off seperator fully automatic operation.
Specific control method includes the following steps:(1), filtering control:Filtering control:When fluid concentration is more than setting highest
After concentration, system starts, and PLC drives main motor to start, centrifugal chamber casing rotation, and fluid is passed through cylinder by PLC driving pump startups
Fluid nozzle is pumped into centrifugal chamber casing, the input oil liquid pressure of pressure sensor detection pump so that the input hydraulic pressure of pump is
0.3MPa;(2), dehydration control:PLC control pumps shut down, and the rotating speed that the first frequency converter is controlled by PLC is 3080 RPM-
3120 RPM;(3), cleaning control:When fluid concentration reach setting minimum concentration after PLC transfer tubes start to work, by new oil,
Liquid is driven into centrifugal chamber casing, removes the internal remaining sludge not peeled off.
The detection of fluid concentration is realized by the strength of fluid sensor in oil sump in filtering control in the present invention,
The strength of fluid sensor is equipped with two threshold values of maximum concentration and minimum concentration, strength of fluid sensor after reaching either threshold
It is fed back to PLC, touches and acts in next step.
The present invention will be further described with reference to the accompanying drawings and embodiments.
Embodiment 1:Full-automatic fluid removes the gred seperator, it include pedestal, shell, main motor, auxiliary motor, centrifugal chamber casing,
Clinker collecting box and removing device, removing device are located inside centrifugal chamber casing, include close to the scraper 9 of centrifugal chamber casing inner wall and suitable
The air-leg 10 that drives scraper centrifugal chamber in move horizontally affixed with scraper in shell is fitted over, is arranged in centrifugal chamber casing
There are cylindrical fluid nozzle and fluid outlet, cylindrical fluid nozzle to be in communication with the outside by pump, signal connects on the main motor
It is connected to PLC and the first frequency converter, signal is connected with strength of fluid sensor on the PLC, and pressure sensing is connected on the pump
Device, the pressure sensor signal are connected with the second frequency converter, and second frequency converter is connect with PLC signals, and the clinker is received
Header is built-in with the weighing sensor being connect with PLC signals.
The control method of full-automatic fluid slagging-off seperator, it includes the following steps:(1), filtering control:PLC transfer tubes
Fluid is pumped by cylindrical fluid nozzle in centrifugal chamber casing by startup, and strength of fluid sensor detects the fluid in centrifugal chamber casing
Concentration, after fluid concentration is more than setting maximum concentration, PLC drives main motor to start, centrifugal chamber casing rotation, pressure sensor inspection
Survey the input oil liquid pressure of pump so that the input hydraulic pressure of pump is 0.3MPa;(2), dehydration control:PLC control pumps shut down, and lead to
It is 3080 RPM to cross PLC and control the rotating speed of the first frequency converter;(3), cleaning control:After fluid concentration reaches setting minimum concentration
PLC transfer tubes are started to work, and new oil, liquid are driven into centrifugal chamber casing, remove the internal remaining sludge not peeled off.
Embodiment 2:Difference lies in there are two the clinker collecting boxs, be spaced apart to connect in PLC signals with embodiment 1
On the conveyer belt connect, the two clinker collecting boxs can be referred to as tight preceding collecting box and next collecting box, one of them is located at gear
The underface of plate.
The control method of full-automatic fluid slagging-off seperator, difference lies in steps with embodiment 1(2)Dehydration control in
The rotating speed that the first frequency converter is controlled by PLC is 3100 RPM, in step(2)Dehydration control and step(3)Between cleaning control
It is more to strike off control:Weighing sensor is weighed to clinker collecting box and is compared with preset desired value in PLC, when more than mesh
PLC controls conveyer belt and the clinker collecting box equipped with sludge is delivered to other stations, the conveying of unloaded clinker collecting box after scale value
Below to centrifugal chamber casing.
Embodiment 3:The difference from example 2 is that there are three the clinker collecting boxs, it is spaced apart and connects in PLC signals
On the conveyer belt connect.
The control method of full-automatic fluid slagging-off seperator, the difference from example 2 is that step(2)Dehydration control in
The rotating speed that the first frequency converter is controlled by PLC is 3120 RPM.
Why the present invention controls the input hydraulic pressure of pump in 0.3MPa, is in order to avoid because strength of fluid or medium are former
Fuel transfer pressure is excessively high too low caused by, and pass through the study found that if hydraulic pressure less than 0.3 MPa can cause pump input fluid without
Method is sprayed in centrifugal rotor, if pressure is higher than 0.3MPa, the radial load of pump can be caused excessive, specific data see the table below:
Table 1
Research it has also been found that, under the premise of the input hydraulic pressure of pump is controlled in 0.3MPa, under identical particulate matter best dehydrating speed and
The relationship of electric current see the table below:
Table 2
It can be seen that dehydrating effect is bad when the rotating speed of the first frequency converter is less than 3080RPM, and it is slight sticky, when turning for the first frequency converter
Electric current is excessive when speed is higher than 3120RPM, influences the working life of frequency converter.
The present invention realizes the Automatic Control requirement for the seperator that removes the gred for fluid, stable, reliable, reduces manpower
Cost simultaneously reduces the consumption of the unnecessary operation in daily production.The dynamic monitoring to fluid is realized, and is being pinpointed the problems
Afterwards, maintenance policy information can be pushed in time, prevent problem worse, high degree of automation.
Claims (5)
- The seperator 1. full-automatic fluid removes the gred, it includes pedestal (1), shell (2), main motor (3), auxiliary motor (4), centrifugal chamber casing (5), clinker collecting box(13)And removing device, cylindrical fluid nozzle is provided in centrifugal chamber casing(6)It is exported with fluid(7), Cylindrical fluid nozzle passes through pump(8)It is in communication with the outside, it is characterized in that signal is connected with PLC on the main motor(14)With first Frequency converter(15), signal is connected with strength of fluid sensor on the PLC(17), pressure sensor is connected on the pump (16), the pressure sensor signal is connected with the second frequency converter(18), second frequency converter is connect with PLC signals, described Clinker collecting box is built-in with the weighing sensor being connect with PLC signals(19).
- The seperator 2. fluid as described in claim 1 full-automatic removes the gred, it is characterized in that the clinker collecting box at least there are two, On the conveyer belt being connect with PLC signals.
- The seperator 3. full-automatic fluid as described in claim 1 removes the gred, it is characterized in that the removing device is located at centrifugal chamber casing Inside includes the scraper close to centrifugal chamber casing inner wall(9)With fit in shell with scraper it is affixed drive scraper from The air-leg moved horizontally in the chambers of the heart(10).
- 4. the control method of the full-automatic fluid slagging-off seperator as described in claim 1 or 3, it is characterized in that it includes following step Suddenly:(1), filtering control:After fluid concentration is more than setting maximum concentration, system starts, and PLC drives main motor to start, centrifugation Cavity rotates, and fluid is pumped by cylindrical fluid nozzle in centrifugal chamber casing by PLC driving pump startups, pressure sensor detection pump Input oil liquid pressure so that the input hydraulic pressure of pump be 0.3MPa;(2), dehydration control:PLC control pumps shut down, and pass through The rotating speed that PLC controls the first frequency converter is 3080 RPM-3120 RPM;(3), cleaning control:When fluid concentration reaches setting most PLC transfer tubes are started to work after low concentration, and new oil, liquid are driven into centrifugal chamber casing, remove what internal residue was not peeled off Sludge.
- 5. the control method of full-automatic fluid slagging-off seperator as claimed in claim 2, it is characterized in that it includes the following steps: (1), filtering control:After fluid concentration is more than setting maximum concentration, system starts, and PLC drives main motor to start, centrifugal chamber casing Fluid is pumped by cylindrical fluid nozzle in centrifugal chamber casing by rotation, PLC driving pump startups, and pressure sensor detects fluid pressure Power and with the operating of the first frequency converter and the second frequency converter coordinated signals main motor and pump so that the hydraulic pressure in centrifugal chamber casing is 0.3MPa;(2), dehydration control:PLC control pumps shut down, and the rotating speed that the first frequency converter is controlled by PLC is 3080 RPM- 3120 RPM;(3), strike off control:Weighing sensor weighed to clinker collecting box and with preset desired value ratio in PLC Right, PLC controls conveyer belt and the clinker collecting box equipped with sludge is delivered to other stations, unloaded clinker after more than desired value Collecting box is delivered to below centrifugal chamber casing;(4), cleaning control:PLC transfer tubes are opened after fluid concentration reaches setting minimum concentration New oil, liquid are driven into centrifugal chamber casing by beginning work, remove the internal remaining sludge not peeled off.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810263615.1A CN108620241A (en) | 2018-03-28 | 2018-03-28 | Full-automatic fluid slagging-off seperator and its control method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810263615.1A CN108620241A (en) | 2018-03-28 | 2018-03-28 | Full-automatic fluid slagging-off seperator and its control method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108620241A true CN108620241A (en) | 2018-10-09 |
Family
ID=63696546
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810263615.1A Pending CN108620241A (en) | 2018-03-28 | 2018-03-28 | Full-automatic fluid slagging-off seperator and its control method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108620241A (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102350402A (en) * | 2011-06-02 | 2012-02-15 | 江苏巴威工程技术股份有限公司 | Control system of centrifugal oil purification device |
CN103056041A (en) * | 2012-12-12 | 2013-04-24 | 镇江市科能电力设备有限公司 | Remote control device of centrifugal machine |
CN203448197U (en) * | 2013-08-20 | 2014-02-26 | 成都西部石油装备有限公司 | Novel control system for centrifuge |
CN204699846U (en) * | 2015-04-27 | 2015-10-14 | 北京岳能科技股份有限公司 | A kind of fluid essence filter system |
CN105195336A (en) * | 2015-09-11 | 2015-12-30 | 安徽科利恩洁油环保设备有限公司 | Automatic slag removal and separation machine for oil and fluids |
WO2016025590A1 (en) * | 2014-08-12 | 2016-02-18 | Water Planet, Inc. | Intelligent fluid filtration management system |
CN205128203U (en) * | 2015-10-21 | 2016-04-06 | 上海市离心机械研究所有限公司 | Centrifugal separator network control system based on industrial ethernet |
-
2018
- 2018-03-28 CN CN201810263615.1A patent/CN108620241A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102350402A (en) * | 2011-06-02 | 2012-02-15 | 江苏巴威工程技术股份有限公司 | Control system of centrifugal oil purification device |
CN103056041A (en) * | 2012-12-12 | 2013-04-24 | 镇江市科能电力设备有限公司 | Remote control device of centrifugal machine |
CN203448197U (en) * | 2013-08-20 | 2014-02-26 | 成都西部石油装备有限公司 | Novel control system for centrifuge |
WO2016025590A1 (en) * | 2014-08-12 | 2016-02-18 | Water Planet, Inc. | Intelligent fluid filtration management system |
CN204699846U (en) * | 2015-04-27 | 2015-10-14 | 北京岳能科技股份有限公司 | A kind of fluid essence filter system |
CN105195336A (en) * | 2015-09-11 | 2015-12-30 | 安徽科利恩洁油环保设备有限公司 | Automatic slag removal and separation machine for oil and fluids |
CN205128203U (en) * | 2015-10-21 | 2016-04-06 | 上海市离心机械研究所有限公司 | Centrifugal separator network control system based on industrial ethernet |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106399639A (en) | Dry type mechanical vacuum pump degassing system and method for liquid steel secondary refining | |
CN203091369U (en) | Automatic mechanical cleaning device of product oil storage tank | |
CN107382011A (en) | Sludge press filtration processing system and sludge press filtration processing method | |
CN102476994B (en) | Method for filtering, washing and separating crude terephthalic acid by using oxidizing unit of fine terephthalic acid device | |
CN103497777A (en) | Heavy oil and bitumen extraction and separation method from coal-based oil residue | |
CN104147825A (en) | Energy-saving solid state feed device based on charging characteristic of filter press and method thereof | |
CN106597986B (en) | Control device and method for double-stage pushing centrifugal machine based on PID | |
CN108620241A (en) | Full-automatic fluid slagging-off seperator and its control method | |
CN102120100B (en) | Process and device for continuously extracting supercritical CO2 in flat turn manner | |
CN107225091A (en) | The method of work of industrial processes screening plant | |
CN213912922U (en) | Flame-retardant type sintering furnace high vacuum filter capable of automatically cleaning ash on line | |
CN212387306U (en) | Carbon black pneumatic conveying system of double-combination dust remover | |
CN110801669A (en) | Three-phase separation system and method with self-cleaning and residue dewatering functions | |
CN210845530U (en) | Filtrate centrifugal separation device for extracting 1-deoxynojirimycin from mulberry leaves | |
CN210545737U (en) | Solid-liquid separation equipment for lubricating oil production | |
CN210065700U (en) | Production facility of continuous type negative pressure wind drenches low temperature and squeezes vegetable oil | |
CN203079912U (en) | Dust-containing coal tar separation equipment | |
CN115301703B (en) | Kitchen waste pulping and sorting system and operation method thereof | |
CN111097745A (en) | Environment-friendly automatic cleaning and processing integrated equipment | |
CN109401832B (en) | Full-automatic intelligent amortization formula oil extraction production system | |
CN102989233A (en) | Continuous filtration method for polyacrylonitrile pulp | |
CN202297733U (en) | Sintering waste heat recovery and sintering main exhaust fan combined driving unit | |
CN218232116U (en) | Petrochemical electro-desalting oily sewage comprehensive treatment system | |
CN210474948U (en) | A dehydration treatment device for kitchen garbage anaerobic digestion natural pond sediment | |
CN208758321U (en) | Restaurant garbage treating system |
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 | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181009 |
|
RJ01 | Rejection of invention patent application after publication |