CN1313895C - Method and system for controlling coagulant filling rate by on-line measuring flocculate sedimentation speed - Google Patents
Method and system for controlling coagulant filling rate by on-line measuring flocculate sedimentation speed Download PDFInfo
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- CN1313895C CN1313895C CNB2005100272721A CN200510027272A CN1313895C CN 1313895 C CN1313895 C CN 1313895C CN B2005100272721 A CNB2005100272721 A CN B2005100272721A CN 200510027272 A CN200510027272 A CN 200510027272A CN 1313895 C CN1313895 C CN 1313895C
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Abstract
The present invention relates to a method and a system for controlling coagulant filling rate by measuring flocculate sedimentation speed on line, and in the method for controlling coagulant filling rate by measuring flocculate sedimentation speed on line, the coagulant filling rate is controlled by measuring the flocculate sedimentation speed on line. The method for controlling coagulant filling rate by measuring flocculate sedimentation speed on line comprises the following steps: (1) one flocculate moving image is collected every 0.5 second, and the position of flocculate is calculated; (2) the flocculate sedimentation speed is calculated according to the position change of the flocculate; (3) the detected flocculate sedimentation speed is compared with a target value, and then the coagulant filling rate is determined. A sensing head of a flocculate image collecting sensor of the system for controlling coagulant filling rate by measuring flocculate sedimentation speed on line is improved so as to be suitable for the measurement of the flocculate sedimentation speed. The present invention tries to control the filling rate by measuring a single parameter, and the method for controlling coagulant filling rate by measuring flocculate sedimentation speed on line is direct and effective.
Description
Technical field
The present invention is a kind of method and system of realizing the automatic control of coagulant filling by on-line measurement floc unit settling velocity.Belong to the water supply engineering field.
Background technology
The filling coagulant is liquid in the present water treatment procedure, separates the most frequently used method admittedly.Whether adding amount appropriately is directly connected to dispatch from the factory water quality and production cost.The automatic control of adding amount is one of key link of water process automation, also is the problem that solves of not improving as yet in the current water process automation.
In the water factory system water, whether coagulant dosing is appropriate, and generally whether turbidity remains on about a certain desired value is Rule of judgment with settling basin water outlet (hereinafter to be referred as precipitation water).Desired value is to require to determine with the rejection rate in filter tank according to the turbidity of filtering back water.Desired value is too big, does not reach the turbidity requirement of filter back water, the too little consumption that then can increase coagulant.
Along with the raising of the development of society, living standards of the people with to the concern of self health, more and more higher to the domestic water requirements in water quality.Be in the control water harmful protozoas such as recessive sporozoite, the U.S. has required delivery turbidity less than 0.3NTU (NTU is a turbidity unit, 1NTU roughly be equivalent to impurity content is 1ppm in the water) at present, and Japan requires less than 0.1NTU.This is just more strict to the processing requirements before precipitating, and is also stricter to the control requirement of coagulant dosing.
Just right automatic control adding amount both can reach the purpose that guarantees water quality, can improve automaticity again, reduced operating personnel, reduced the consumption of coagulant, reduced production costs.Water factory's amount multiaspect of China is wide, and because of the defective of present autocontrol method and equipment, the overwhelming majority adopts manual control, if can adopt effective, adaptable autocontrol method and equipment, and its economic and social benefit will be huge.
The factor that influences coagulant dosing is very many, and these factors are constantly changing.The for example turbidity in the raw water quality, water temperature, flow, basicity, ammonia nitrogen, oxygen utilization, the load of purifier, state etc. also have considerable part factor also not fully aware of at present.Therefore throwing in coagulant accurately, rightly is a very complicated problems.In addition, coagulant filling is a long delay system (2-3 hour) through mixing, flocculate, precipitating, and can't obtain good control performance with general aim parameter closed-loop control.Therefore on control method and detection parameter, carried out many research work both at home and abroad, several different methods has also been arranged.By length retardation time that detects parameter, be broadly divided into prediction in early stage and medium-term forecast control two big classes:
(1). prediction in early stage (feedforward) control: this method is according to the raw water quality parameter, and the prediction coagulant dosing makes the precipitation water turbidity reach predetermined value.Early stage, PREDICTIVE CONTROL did not have retardation time.As long as mathematical model is enough accurate, this method can be eliminated raw water quality fully and change the deviation that causes theoretically.But coagulation process is complicated, the parameter that influences coagulant dosing is very many, can't obtain mathematical model accurately in theory, consider the complexity of system in the practical application again, the feasibility of parameter on-line testing and complexity, order of accuarcy, therefore be difficult to guarantee the comprehensive of parameter and mathematical model, generally can only select several main parameters such as flow, turbidity, temperature, basicity, pH value etc., this is enough substantially for cleaner water, but, just can't only represent with these parameters for the water that is subjected to organic pollutants.But will catch this moment the parameter of several METHOD FOR CONTINUOUS DETERMINATION to represent the filling rate of coagulant substantially, be quite difficult problem.For overcoming the above problems, also used modern control method such as fuzzy logic, self-adaptation, artificial neural network in recent years both at home and abroad, though improving the control effect in varying degrees, the weakness of this method is not eliminated.Too many because of the parameter of measuring simultaneously, for improving the security of supplying water, the people is arranged even studied the problem that when a certain parameter measurement equipment has fault, how to reduce departure.Stack up says that this method can eliminate the deviation that the variation of raw water quality causes in perfect condition, but can not eliminate the deviation that the purifier state variation causes.In the practical application, the equipment price of some parameter on-line testing is higher, and difficult in maintenance, some parameter at present also can't on-line measurement or accuracy low, influenced the control effect.
(2). medium-term forecast (middle feedback) control: the parameter behind the measurement coagulant filling, prediction settling basin delivery turbidity is adjusted coagulant dosing thus.Though this method has hysteresis, prediction accurately and the degree of reliability generally be better than first method, main method has:
1. simulation settling basin method: the overwhelming majority of water cleaning systems retardation time is produced by settling basin, therefore can simulate settling basin with inclined tube or model filter tank, reduces retardation time.But their simulation degree is not high, is subject to the influence of other factors yet.
2. streaming current is measured (SCD) method: measuring streaming current is a kind of method of measuring Zeta potential indirectly, and Zeta potential is then relevant with flocculating conditions.This is the more a kind of method of using both at home and abroad in recent years.Its retardation time is very short, is incorporation time.The successful report of many uses is arranged, but also have unfavorable.When some interfering material is arranged in the water, have bigger deviation between measured value and the rational adding amount.Dental thinks: the SC value just is directly proportional with Zeta potential and is based upon on the perfect condition, and the representative water sample of promptly coming in sticks on the piston face of probe, and fully topped on piston face, the electrical interference that nobody is.This supposition can not be satisfied sometimes, so result of use is not good sometimes.During change of water quality, also need adjust setting value in addition.For improving control performance, the someone uses SCD to add that other parameters carry out fuzzy logic control.
3. flocculation detection method: closely related because of precipitating water turbidity and flocculating effect, this method detects flocculating effect, and whether prediction precipitation water turbidity is appropriate to determine coagulant filling.Be mixing, reaction time its retardation time.Having comprised the influence of reaction tank duty in this method testing result, is a kind of method preferably, and key is selected parameter and the degree of correlation that precipitates water turbidity.Concrete grammar has:
(1) transmittance pulsation flocculation detection method: principle is to pass through a branch of light time when flco suspending liquid, the transmission light intensity changes, calculate the mean square value that transmitted light changes and the ratio of DC component, certain condition can be represented the size of flco down, available it control the coagulant filling rate.This method measuring equipment is simple, and cost is low, but its measured value is relevant with raw water turbidity, and the stability of reading is also undesirable.
(2) optical scatter analyser (PDA) and optical particulate number scale: by analyzing floc unit scattered light signal or floc unit shielding signals, obtain the information relevant, be used to control adding amount with the grain size of flocculating.
(3) floc unit test pattern method: this is applicant's a achievement in research, has obtained patent of invention (ZL98110624.2).Method is to obtain and handle the flco graphical information in real time, according to size, shape and the distribution situation (these parameters are relevant with settling velocity) of flco, controls the coagulant filling rate.This method quantitative measurement coagulation effect, measured value is stable and irrelevant, more directly perceived and accurate with raw water turbidity, and is fine with the correlativity of settling basin delivery turbidity under the normal condition, uses in water factory.But in the former water organism more for a long time, this method can not reflect that flco lightens, the situation that settling velocity is slack-off.
Above the whole bag of tricks respectively has its relative merits and certain scope of application, but perfect far away, so research effect is better, the scope of application is wider, and operating ratio is more convenient, and cost is relatively low, safeguard fairly simple tested parameter and control mode, be still present exigence.
Summary of the invention
The object of the present invention is to provide a kind of method and system by on-line measurement flco settling velocity control coagulant dosing, control adding amount to measure single parameter as far as possible, detection method is more direct, effective.
For achieving the above object, design of the present invention is:
The key that improves the control effect is what parameter to predict settling basin delivery turbidity (hereinafter to be referred as the precipitation water turbidity) according to, thus the control adding amount.This parameter should be clear and definite with precipitation water turbidity relation, and single as far as possible (being affected by other factors less), and retardation time is shorter, simultaneously this parameter should by accurately, online detection stably.
General thought: under certain deposition condition, the quality of coagulation is closely related with the precipitation water turbidity, the purpose that adds coagulant is exactly the granule in the water to be condensed into proportion precipitate greater than the bulky grain of water, so the essence of coagulation quality shows the settling velocity of floc unit particle.Settling velocity can precipitate in settling basin greater than the floc unit (hereinafter to be referred as flco) of certain numerical value, settling velocity is at the flco of a certain scope, though can not directly precipitate, in settling basin, collide the chance of combination in addition, there is certain ratio in settling basin, to precipitate.Measure the flco settling velocity and take another step than measuring flco area and shape, the condense effect of key factors such as tightness degree, water temperature of proportion, the flco that the former has comprised the floc particle that the latter did not comprise, can be more directly and represent the effect of coagulation, prediction precipitation water turbidity exactly.Control coagulant dosing with it, though certain hysteresis is also arranged, should be than existing other flocculation detection methods all directly with effective.
According to above-mentioned design, the present invention and employing following technical proposals:
A kind of method by on-line measurement flco settling velocity control coagulant dosing, comprise that former water enters mixed reaction pond (10) and mixes with the coagulant that adds, reaction, flocculate and the generation flco, gather floc image in real time by floc image sensor (9) under water at mixed reaction pond (10), view data is machine (8) digital filtering as calculated, the figure image intensifying, image binaryzation is handled, remove and disturb and noise, calculate with flco related parameter is arranged, and with this numerical value with compare from scale value, its difference is after the PID computing, obtain required filling rate, be multiplied by the into flow of water again, obtain adding amount, convert the adding amount of normalized current output signal control dispenser pump (3) to; It is characterized in that it is flco weighted mean settling velocity that described and flco have related parameter, the value of comparing with described flco weighted mean settling velocity is the desired value of weighted mean settling velocity; The desired value of above-mentioned weighted mean settling velocity, be poor by precipitation measured value of water turbidity and setting value, obtain through the digital PID computing, because of deposition condition change generally slower, so the correction of the desired value of weighted mean settling velocity was carried out once in per 30 minutes; Mensuration, the computing method step of flco weighted mean settling velocity are as follows:
(1) described computing machine (8) software design becomes the per 0.5 second terminal data of flco live image under water of collection one width of cloth mixed reaction pond (10), machine carries out described digital filtering, figure image intensifying, image binaryzation processing as calculated, remove the noise that disturbs, thereby form the video data block of binaryzation, calculate the position at each flco place in the image;
(2) computing machine is according to the variation of the same flco of front and back different images position, follow the tracks of the movement locus of each flco, the difference of upright position and used time when calculating its inflow and flowing out the sampling window of floc image sensor (9) sensing head, calculate the settling velocity of each flco: the position when establishing flco inflow sampling window is Y1, position when flowing out sampling window is Y2, be provided with 18 width of cloth images, then the time is 18 * 0.5=9 second, and settling velocity is (Y2-Y1)/9;
(3), calculate the weighted mean settling velocity of the flco of all process sampling windows in per 5 minutes according to the settling velocity of each flco and its size.
Above-mentioned computing machine (8) with per 5 minutes once, compare with weighted mean settling velocity and desired value, its difference is after the PID computing, determine required filling rate, be multiplied by the into flow of water again, obtain adding amount, and convert the normalized current output signal to, control dispenser pump (3) by computing machine (8).
All input and output parameters of above-mentioned computing machine (8), comprise ratio, integration, differential parameter in the PID computing, initial adding amount, the setting value of the desired value of the contrast of image, brightness and settling velocity, precipitation water turbidity, all on screen, show in real time, all can on screen, be provided with voluntarily with pull-down menu; Per 5 minutes computing machine (8) automatically with each parameter of water quality, the desired value that comprises flow of inlet water, adding amount, flco settling velocity and the setting value of measured value, precipitation water turbidity and measured value and date, time deposit hard disk in, as database, prepare against and call.
Be to improve the adaptability of system, above-mentioned computing machine (8) but Control Software be designed to input parameter amount type selecting, except that the flco settling velocity is necessary measurement parameter, comprise that other parameters of precipitation water turbidity, flow, influent turbidity are optional parameter; Input parameter is controlled effective for a long time, and response is fast; Input parameter weak effect after a little while is a little, but can adapt to the occasion that some on-line detector table lacks.
The system that a kind of said method is used, comprise computing machine (8), dispenser pump (3), mixed reaction pond (10) and floc image pick-up transducers (9), it is characterized in that described floc image pick-up transducers (9) is positioned in the terminal water of described mixed reaction pond (10); Described floc image pick-up transducers (9) is designed to: its sensing head comprises subsurface water current guiding reducing gear, and this mechanism makes sluggish flow and steadily and with horizontal direction, no vertical direction current component, the sampling window in the flow path sensing head.
The area of the sampling window of above-mentioned floc image pick-up transducers (9) sensing head is about 30 * 20mm, and thick 3mm is in order to avoid overlapping in the flco plane picture; The flow through horizontal velocity of sampling window of current is controlled at 3mm/S ± 0.5mm/S, and flow through time of sampling window of flco is about 10S.
The present invention is flood dragon compared with prior art, have following conspicuous outstanding substantive distinguishing features and remarkable advantage: the present invention is with this single parameter of on-line measurement flco settling velocity, control the adding amount of coagulant, remove to control the adding amount of coagulant than many reference amounts such as the area of the number that adopts the on-line measurement floc particle in original technology, each flco, girth, length breadth ratio, middle hole areas, detect more directly, more effective, this single parameter can be accurately, online detection stably.The used system of the present invention has carried out particular design to the sensing head of floc image sensor, helps detecting the flco change in location and goes out the flco settling velocity by COMPUTER CALCULATION; The program design of computing machine is also corresponding has done improvement.
Description of drawings
Fig. 1 is that flco settling velocity of the present invention is calculated the floc image synoptic diagram of finding a view with sampling window.
Fig. 2 is a control method block diagram of the present invention.
Fig. 3 is a system architecture diagram of the present invention.
Embodiment
Details are as follows in conjunction with the accompanying drawings in a preferred enforcement of the present invention:
This method by on-line measurement flco settling velocity control coagulant dosing is described below.
1, Yuan Shui enters mixed reaction pond, mixes, reacts, flocculates with the coagulant that adds, and produces flco.This method is at the live image of gathering flco under water by the floc image pick-up transducers in real time of mixed reaction pond end.
2, sensing head comprises subsurface water current guiding, the reducing gear of a particular design, makes the sampling window in sluggish flow, steady (flco can be broken), horizontal direction (the no vertical direction current component) sensing head of flowing through.
3, the about 30*20mm of sampling window area, thickness 3mm is in order to avoid flco is overlapping in plane picture; The flow through horizontal velocity of sampling window of current is controlled at about 3mm/s, and flow through time of sampling window of flco is about 10s.
4, image in the camera picked-up sampling window, and be presented on the graphoscope; Computing machine was gathered the data of piece image in per 0.5 second, then, through the processing of digital filtering, figure image intensifying, image binaryzation, removed and disturbed and noise, formed the video data block of binaryzation, calculated the position at each flco place in the image.
5, computing machine is followed the tracks of the movement locus of each flco according to the variation of the position at the same flco of front and back different images place, the difference of upright position and used time when calculating its inflow and flowing out sampling window, can obtain the settling velocity of each flco.See shown in Figure 1ly, suppose that the flco of being followed the tracks of represents with black, the position when flowing into sampling window is Y1, and (18 width of cloth images are after promptly 9 seconds) are Y2 when flowing out sampling window, and settling velocity is (Y2-Y1)/9.
6,, calculate the weighted mean settling velocity of the flco of all process sampling windows in per 5 minutes according to the settling velocity of each flco and its size.
7, per 5 minutes once, compare with weighted mean settling velocity and desired value, its difference is after the digital PID computing, determine required filling rate, be multiplied by the into flow of water again, obtain adding amount, and convert the normalized current output signal to by computing machine, and control dispenser pump, see shown in Figure 2.
8, the desired value of weighted mean settling velocity is poor by precipitation measured value of water turbidity and setting value, arriving after the digital PID computing.Generally slower because of the deposition condition variation, so the correction of the desired value of average settling velocity was carried out once in per 30 minutes, see shown in Figure 2.
9, all input parameters and output parameter all show on screen in real time.In order to adapt to different water quality, different water factory's actual production technology, the situation of equipment, P in the PID computing (ratio), I (integration), D (differential) parameter, initial adding amount, the setting value of the desired value of the contrast of image, brightness and settling velocity, precipitation water turbidity all can be provided with pull-down menu on screen voluntarily.Per in addition 5 minutes computing machines are automatically with each parameter of water quality, deposit hard disk in as the setting value of the desired value of flow of inlet water, adding amount, flco settling velocity and measured value, precipitation water turbidity and measured value and date, time, as database, prepare against and call.
10, be the adaptability of raising system, but Control Software is designed to import the parameter type selecting, exactly except that the flco settling velocity is necessary detected parameters, other parameter is an optional parameter as precipitation water turbidity, flow, influent turbidity etc.Input parameter is controlled effective for a long time, and response is fast; Though parameter effect after a little while is weaker, also can work, to adapt to the unit that those also do not have these parameter on-line detector tables at present.The structure of the system that said method is used
Fig. 3 is a structured flowchart of realizing the coagulant filling automatic control system according to present embodiment by on-line measurement flco settling velocity.
The structure of system is: water inlet is connected in intake pump 1 import, and outlet connects a flowmeter 2, and mixed reaction pond 10 is connected in flowmeter 2 outlets, and mixed reaction pond 10 outlets are communicated with settling basin 11 imports; Floc image pick-up transducers 9 in water of the terminal installation of mixed reaction pond, the output of this sensor 9 connects computing machines 8 through image interface 6; The control circuit of dispenser pump 3 is connected in the import that 4 outlets of coagulant pond are connected mixed reaction pond 10 through dispenser pump 3, computing machine 8 through IO interface 5; Connect nephelometer 12 on settling basin 11 export pipelines, the output of flowmeter 2 and nephelometer 12 all is connected computing machine 8 through IO interface 5; Computing machine 8 connects a display screen 7.
Claims (6)
1. method by on-line measurement flco settling velocity control coagulant dosing, comprise that former water enters mixed reaction pond (10) and mixes with the coagulant that adds, reaction, flocculate and the generation flco, gather floc image in real time by floc image sensor (9) under water at mixed reaction pond (10), view data is machine (8) digital filtering as calculated, the figure image intensifying, image binaryzation is handled, remove and disturb and noise, calculate with flco related parameter is arranged, and compare with this numerical value and desired value, its difference is after the PID computing, obtain required filling rate, be multiplied by the into flow of water again, obtain adding amount, convert the adding amount of normalized current output signal control dispenser pump (3) to; It is characterized in that it is flco weighted mean settling velocity that described and flco have related parameter, the value of comparing with described flco weighted mean settling velocity is the desired value of weighted mean settling velocity; The desired value of described weighted mean settling velocity is poor by precipitation measured value of water turbidity and setting value, obtain through the digital PID computing, because of deposition condition change generally slower, so the correction of the desired value of average settling velocity was carried out once in per 30 minutes; Mensuration, the computing method step of flco weighted mean settling velocity are as follows:
(1) described computing machine (8) software design becomes the per 0.5 second terminal data of flco live image under water of collection one width of cloth mixed reaction pond (10), machine carries out described digital filtering, figure image intensifying, image binaryzation processing as calculated, remove the noise that disturbs, thereby form the video data block of binaryzation, calculate the position at each flco place in the image;
(2) computing machine is according to the variation of the same flco of front and back different images position, follow the tracks of the movement locus of each flco, the difference of upright position and used time when calculating its inflow and flowing out the sampling window of floc image sensor (9) sensing head, calculate the settling velocity of each flco: the position when establishing flco and going into sampling window is Y1, position when flowing out sampling window is Y2, be provided with 18 width of cloth images, then the time is 18 * 0.5=9 second, and settling velocity is (Y2-Y1)/9;
(3), calculate the weighted mean settling velocity of the flco of all process sampling windows in per 5 minutes according to the settling velocity of each flco and its size.
2. the method by on-line measurement flco settling velocity control coagulant dosing according to claim 1, it is characterized in that described computing machine (8) with per 5 minutes once, compare with weighted mean settling velocity and desired value, its difference is after the PID computing, determine required filling rate, be multiplied by the into flow of water again, obtain adding amount, and convert the normalized current output signal to by computing machine (8), control dispenser pump (3).
3. the method by on-line measurement flco settling velocity control coagulant dosing according to claim 1, all input and output parameters that it is characterized in that described computing machine (8), comprise ratio, integration, differential parameter in the PID computing, initial adding amount, the setting value of the desired value of the contrast of image, brightness and settling velocity, precipitation water turbidity, all on screen, show in real time, all can on screen, be provided with voluntarily with pull-down menu; Per 5 minutes computing machine (8) automatically with each parameter of water quality, the desired value that comprises flow of inlet water, adding amount, flco settling velocity and the setting value of measured value, precipitation water turbidity and measured value and date, time deposit hard disk in, as database, prepare against and call.
4. the method by on-line measurement flco settling velocity control coagulant dosing according to claim 1, it is characterized in that for improving the adaptability of system, described computing machine (8) but Control Software be designed to input parameter amount type selecting, except that the flco settling velocity is necessary measurement parameter, comprise that other parameters of precipitation water turbidity, flow, influent turbidity are optional parameter; Input parameter is controlled effective for a long time, and response is fast; Input parameter weak effect after a little while is a little, but can adapt to the occasion that some on-line detector table lacks.
5. one kind according to the described system that uses by on-line measurement flco settling velocity control coagulant filling metering method of claim 1, comprise computing machine (8), dispenser pump (3), mixed reaction pond (10) and floc image pick-up transducers (9), it is characterized in that described floc image pick-up transducers (9) is positioned in the terminal water of described mixed reaction pond (10); Described floc image pick-up transducers (9) is designed to: its sensing head comprises subsurface water current guiding reducing gear, and this mechanism makes sluggish flow and steadily and with horizontal direction, no vertical direction current component, the sampling window in the sensing head of flowing through.
6. the system by on-line measurement flco settling velocity control coagulant dosing according to claim 5, the area that it is characterized in that the sampling window of described floc image pick-up transducers (9) sensing head is about 30 * 20mm, and thick 3mm is in order to avoid overlapping in the flco plane picture; The horizontal velocity of current flow path sampling window is controlled at 3mm/S ± 0.5mm/S, and the time of flco flow path sampling window is about 10S.
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| WO2021186992A1 (en) * | 2020-03-17 | 2021-09-23 | オルガノ株式会社 | Water treatment system, control device, water treatment method, and program |
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|---|---|---|---|---|
| WO2021186992A1 (en) * | 2020-03-17 | 2021-09-23 | オルガノ株式会社 | Water treatment system, control device, water treatment method, and program |
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| CN1715201A (en) | 2006-01-04 |
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