CN1557737A - Intelligent flocculation chemical dosing system - Google Patents
Intelligent flocculation chemical dosing system Download PDFInfo
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- CN1557737A CN1557737A CNA2004100135274A CN200410013527A CN1557737A CN 1557737 A CN1557737 A CN 1557737A CN A2004100135274 A CNA2004100135274 A CN A2004100135274A CN 200410013527 A CN200410013527 A CN 200410013527A CN 1557737 A CN1557737 A CN 1557737A
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Abstract
The intelligently controlled flocculant throwing system includes central control cabinet, flocculant throwing pump, flow meter, raw water nephelometer, clear water nephelometer, mixer, intermediate parameter instrument and reaction pool, precipitation pool connected via pipeline. The present invention has the capacity of detecting fast the water quality and flocculation degree, adopting several kinds of flocculant and operating manually or automatically, and the system is stable and low in cost.
Description
Technical field: the invention belongs to a kind of water treatment system, specifically relate to a kind of flocculation administration system of intelligent control.
Background technology: aspect the automatic control of unit for treating water link, flocculation dispensing technology is the link of most critical.Flocculation dispensing technology is a complex physicochemical process, so flocculation dispensing technology is process procedure the most rambunctious.The dosage of flocculation agent is the determinative that influences flocculating effect, and medicament expense accounts for very big ratio in the cost of harnessing the river, and regulate dosage timely and accurately to adapt to the variation of raw water quality and operational conditions, reach with minimum medicine consumption and obtain the important topic that the decontamination effect improving that meets the demands has just become the water treatment link.Utilize the conventional simulation laboratory method that water quality and former water flocculation situation are monitored or controlled, it can not reflect water quality and flocculating degree rapidly, retardation time is long, workload is big, complicated operation, be not suitable for the quick on-line monitoring of water technology and the requirement of control, developed the control that adds that is only applicable to the conventional coagulating agent of electrolytes with the streaming current coagulation administration Controlling System of widespread use, still can not be directly used in the flocculation process that adds the nonelectrolyte series polymeric flocculant and detect and control.The transmittance pulsation detection technology that occurs at the year ends 80, though the change of size of particulate matter in can online detection water, but its technology is immature, exist retardation time long, raw water turbidity change to the default value influence greatly, poor, the system's instability of resemble process and the more high shortcoming of cost.
Summary of the invention: the purpose of this invention is to provide a kind of intelligence flocculation administration system.The present invention can solve that existing water treatment administration system can not detect water quality and flocculating degree rapidly, retardation time is long, spendable coagulating agent kind is single, workload is big, complicated operation, system's instability and the more high shortcoming of cost.It is made up of center housing 1, chemicals feed pump 2, chemicals feed pump 3, under meter 4, raw water turbidity instrument 5, mixing tank 6, clear water turbidimeter 7, reaction tank 8, settling tank 9, water inlet pipe 11, rising pipe 12, drug tube 13; The power drives port one-4 of center housing 1, power drives port one-5 connects the power input mouth 2-2 of chemicals feed pump 2 respectively, the power input mouth 3-2 of chemicals feed pump 3, the data-in port 1-6 of center housing 1, data-in port 1-7, data-in port 1-9 is the data-out port 4-3 of connection traffic meter 4 respectively, the data-out port 5-2 of raw water turbidity instrument 5, the data-out port 7-2 of clear water turbidimeter 7, the medicine outlet 2-1 of chemicals feed pump 2, the medicine outlet 3-1 of chemicals feed pump 3 connects the feeding opening 6-2 end of mixing tank 6 by drug tube 13, the water-in 4-1 of one end connection traffic meter 4 of water inlet pipe 11, the water outlet 4-2 of under meter 4 connects the detection port 5-1 end of raw water turbidity instrument 5 and connects the water-in 6-1 end of mixing tank 6, the water-in 8-1 end in the water outlet 6-3 end ligation pond 8 of mixing tank 6, the water side 8-2 of reaction tank 8 connects the feed-water end 9-1 of settling tank 9, and the water outlet 9-2 end of settling tank 9 connects the detection port 7-1 end of clear water turbidimeter 7 and connects an end of rising pipe 12.Former water is by water inlet pipe 11 under meter 4 of flowing through during operation, during raw water turbidity instrument 5, the turbidity data that 5 pairs of former water gagings of data on flows that under meter 4 is measured and raw water turbidity instrument go out are delivered to and are carried out data operation in the center housing 1, center housing 1 is controlled chemicals feed pump 2 according to operation result, 3 add flocculation agent, flocculation agent in 6 li in mixing tank with former water thorough mixing after intermediate parameters instrument 10 flows into reflection pond 8 after detecting again, in the settling tank 9, clear water in the settling tank 9 flows into rising pipe 12 after the detection of clear water turbidimeter 7, intermediate parameters instrument 10, the detection data of clear water turbidimeter 7 are delivered to the correction computing that participates in flocculant dosage and intermediate parameters set(ting)value in the center housing 1 respectively, to obtain adopting minimum medicine consumption to obtain the decontamination effect improving that meets the demands.The present invention have to the ability of water quality and flocculating degree rapid detection, intelligent degree height, simple to operate, can use multiple coagulating agent, also manually operation automatically, system stability, cost low.
Description of drawings: Fig. 1 is a structural representation of the present invention, and Fig. 2 is the structural representation of center housing 1, and Fig. 3 is the structural representation of programmable logic controller 1-3, and Fig. 4 is the structural representation of embodiment two.
Embodiment one: in conjunction with Fig. 1, Fig. 2, Fig. 3 present embodiment is described, this embodiment is made up of center housing 1, chemicals feed pump 2, chemicals feed pump 3, under meter 4, raw water turbidity instrument 5, mixing tank 6, clear water turbidimeter 7, reaction tank 8, settling tank 9, water inlet pipe 11, rising pipe 12, drug tube 13; The power drives port one-4 of center housing 1, power drives port one-5 connects the power input mouth 2-2 of chemicals feed pump 2 respectively, the power input mouth 3-2 of chemicals feed pump 3, the data-in port 1-6 of center housing 1, data-in port 1-7, data-in port 1-9 is the data-out port 4-3 of connection traffic meter 4 respectively, the data-out port 5-2 of raw water turbidity instrument 5, the data-out port 7-2 of clear water turbidimeter 7, the medicine outlet 2-1 of chemicals feed pump 2, the medicine outlet 3-1 of chemicals feed pump 3 connects the feeding opening 6-2 end of mixing tank 6 by drug tube 13, the water-in 4-1 of one end connection traffic meter 4 of water inlet pipe 11, the water outlet 4-2 of under meter 4 connects the detection port 5-1 end of raw water turbidity instrument 5 and connects the water-in 6-1 end of mixing tank 6, the water-in 8-1 end in the water outlet 6-3 end ligation pond 8 of mixing tank 6, the water side 8-2 of reaction tank 8 connects the feed-water end 9-1 of settling tank 9, and the water outlet 9-2 end of settling tank 9 connects the detection port 7-1 end of clear water turbidimeter 7 and connects an end of rising pipe 12; Described center housing 1 is made up of variable-frequence governor 1-1, man-machine interface 1-2, programmable logic controller 1-3; The power drives end 1-1-1 of variable-frequence governor 1-1, power drives end 1-1-2 connects the power drives end 1-4 of center housing 1 respectively, power drives end 1-5, the data pin 1-3-1 of programmable logic controller 1-3, data pin 1-3-2, data pin 1-3-4 connects the data input pin 1-6 of center housing 1 respectively, data input pin 1-7, data input pin 1-9, the data communication port 1-2-1 end of man-machine interface 1-2 connects the data communication port 1-3-5 end of programmable logic controller 1-3, and the FPDP 1-3-6 end of programmable logic controller 1-3 connects the FPDP 1-1-3 end of variable-frequence governor 1-1; Described programmable logic controller 1-3 is made up of deviation variation rate computing module 14, obfuscation module 15, performance measurement module 16, manipulated variable correction module 17, control law correcting module 18, fuzzy control rule module 19, fuzzy logic decision module 20, defuzzification module 21, judge module 22, integral control module 23, subtractor 25, multiplier 26; The initial control rules of fuzzy control rule module 19 inside is the historical datas of offeing medicine according to manually, the relational database between the raw water flow detected value of the obfuscation of formation, raw water turbidity detected value, turbidity deviation and the flocculant dosage; Port one-3-5 connects the positive input terminal of subtractor 25, port one-3-4 connects the negative input end of subtractor 25, the output terminal of subtractor 25 connects the input terminus of deviation variation rate computing module 14, the input terminus 151 of obfuscation module 15, the input terminus 221 of judge module 22, the input terminus 222 of the output terminal connection judgment module 22 of deviation variation rate computing module 14, the input terminus 152 of obfuscation module 15, the input terminus 153 of port one-3-2 connection mode gelatinization module 15, the input terminus 154 of port one-3-1 connection mode gelatinization module 15, the input terminus 161 of the output terminal 155 switching performance measurement modules 16 of obfuscation module 15, the input terminus 181 of control law correcting module 18, the input terminus 162 of the output terminal 156 switching performance measurement modules 16 of obfuscation module 15, the input terminus 191 of fuzzy control rule module 19, the output terminal 157 of obfuscation module 15, output terminal 158 connects the input terminus 192 of fuzzy control rule module 19 respectively, input terminus 193, the output terminal 163 of performance measurement module 16 connects the input terminus of manipulated variable correction module 17, the output terminal of manipulated variable correction module 17 connects the input terminus 182 of control law correcting module 18, the output terminal 183 of control law correcting module 18 connects the input terminus 194 of fuzzy control rule module 19, the input terminus of the output terminal 195 connection mode fuzzy logic decision-making modules 20 of fuzzy control rule module 19, the output terminal of fuzzy logic decision module 20 connects the input terminus 211 of defuzzification module 21, the output terminal 223 of judge module 22 connects the input terminus of integral control module 23, the output terminal of integral control module 23 connects the input terminus 261 of multiplier 26, the output terminal 212 of defuzzification module 21 connects the input terminus 262 of multiplier 26, the output terminal connectivity port 1-3-6 end of multiplier 26.Control principle is: the settling tank delivery turbidity value that the last turbidity set(ting)value of setting of man-machine interface 1-2 is deducted 7 detections of clear water turbidimeter obtains turbidity deviation e, and e obtains deviation variation rate Δ e by 14 pairs of time differentiates of deviation variation rate computing module.The raw water flow value of under meter 4 detections, turbidity value, turbidity deviation e and the deviation variation rate Δ e of raw water turbidity instrument 5 detections are input to the input terminus of obfuscation module 15, after handling through obfuscation module 15, the resulting data of processing by fuzzy control rule module 19, fuzzy logic decision module 20, defuzzification module 21 and the data of integral control module 23 outputs multiply each other and become final dosage and control output signal.Wherein performance measurement module 16, manipulated variable correction module 17, control law correcting module 18 are to come self-learning module that the control law of fuzzy control rule module 19 inside is made amendment according to turbidity deviation e and deviation variation rate Δ e.Integral control module 23 adopts conventional integral control algorithm, uses turbidity deviation e value as integration amount.Whether judge module 22 is effective according to the output action of the size decision integral control module 23 of turbidity deviation e and deviation variation rate Δ e value.Chemicals feed pump 2, chemicals feed pump 3 is selected the R series volume pump of German SERA company for use, under meter 4 is selected the FLS100 series flow sensor of FIP company for use, raw water turbidity instrument 5 is selected the SS6 of U.S. HACH company for use, the high turbidimeter of SS6/HST type, clear water turbidimeter 7 is selected the 1720D of U.S. HACH company for use, the 1720D/L type hangs down turbidimeter, mixing tank 6 is selected the duct type static mixer for use, reaction tank 8 is selected grid reaction pond or partition plate reaction tank for use, settling tank 9 is selected inclined tube/inclined-plate clarifying basin or horizontal sedimentation tank for use, variable-frequence governor 1-1 selects the universal VF0 Series Frequency Converter of SUNX for use, man-machine interface 1-2 selects siemens TP070 for use, TP170 series touch-screen or the electricity PPC of Taiwan Weida series panel computer, programmable logic controller 1-3 selects siemens S7-300 for use, S7-200 series Programmable logic Controller (PLC) and expansion module.
Embodiment two: present embodiment is described in conjunction with Fig. 1, Fig. 2, Fig. 3, Fig. 4, this embodiment increases on the basis of embodiment one intermediate parameters instrument 10, and increasing on programmable logic controller 1-3 has intermediate parameters controller module 24, totalizer 27, subtractor 28; Increasing on the fuzzy control rule module 19 based on the relational database between raw water flow detected value, raw water turbidity detected value, turbidity deviation and the intermediate parameters set(ting)value of obfuscation, it is corresponding to the output terminal 213 of defuzzification module 21, and original relational database is corresponding to the output terminal 212 of defuzzification module 21; Intermediate parameters controller 24 adopts conventional proportional integral algorithm, difference according to intermediate parameters set(ting)value and intermediate parameters instrument 10 detected values is carried out the proportional integral computing, and its set(ting)value is revised with the output of integration control module 23 is superimposed automatically by the output terminal 213 of defuzzification module 21; The detection port 10-1 of intermediate parameters instrument 10 connects the water outlet 6-3 end of mixing tank 6 and the water-in 8-1 end in ligation pond 8, the data-in port 1-8 end of the data-out port 10-2 end connection center housing 1 of intermediate parameters instrument 10, the data-in port 1-8 of center housing 1 connects the FPDP 1-3-3 end of programmable logic controller 1-3; The output terminal of integral control module 23 connects the input terminus 271 of totalizer 27, the output terminal 213 of defuzzification module 21 connects the input terminus 272 of totalizer 27, the output terminal 273 of totalizer 27 connects the positive input terminal of subtractor 28, FPDP 1-3-3 connects the negative input end of subtractor 28, the output terminal of subtractor 28 connects the input terminus of intermediate parameters controller module 24, the output terminal of intermediate parameters controller module 24 connects the input terminus 262 of multiplier 26, and the output terminal 212 of defuzzification module 21 connects the input terminus 261 of multiplier 26.It has shortening retardation time, the effect of the dynamic responding speed of enhanced system.Intermediate parameters instrument 10 is selected the SPD1000 type detector of U.S. Sentrol company for use.
Claims (4)
1, intelligence flocculation administration system is characterized in that it is made up of center housing (1), chemicals feed pump (2), chemicals feed pump (3), under meter (4), raw water turbidity instrument (5), mixing tank (6), clear water turbidimeter (7), reaction tank (8), settling tank (9), water inlet pipe (11), rising pipe (12), drug tube (13); The power drives port (1-4) of center housing (1), power drives port (1-5) connects the power input mouth (2-2) of chemicals feed pump (2) respectively, the power input mouth (3-2) of chemicals feed pump (3), the data-in port (1-6) of center housing (1), data-in port (1-7), data-in port (1-9) is the data-out port (4-3) of connection traffic meter (4) respectively, the data-out port (5-2) of raw water turbidity instrument (5), the data-out port (7-2) of clear water turbidimeter (7), the medicine outlet (2-1) of chemicals feed pump (2), the medicine outlet (3-1) of chemicals feed pump (3) connects feeding opening (6-2) end of mixing tank (6) by drug tube (13), the water-in (4-1) of one end connection traffic meter (4) of water inlet pipe (11), the water outlet (4-2) of under meter (4) connects detection port (5-1) end of raw water turbidity instrument (5) and connects water-in (6-1) end of mixing tank (6), water-in (8-1) end in water outlet (6-3) the end ligation pond (8) of mixing tank (6), the water side (8-2) of reaction tank (8) connects the feed-water end (9-1) of settling tank (9), and water outlet (9-2) end of settling tank (9) connects detection port (7-1) end of clear water turbidimeter (7) and connects an end of rising pipe (12).
2, intelligence flocculation administration system according to claim 1 is characterized in that center housing (1) is made up of variable-frequence governor (1-1), man-machine interface (1-2), programmable logic controller (1-3); The power drives end (1-1-1) of variable-frequence governor (1-1), power drives end (1-1-2) connects the power drives end (1-4) of center housing (1) respectively, power drives end (1-5), the data pin (1-3-1) of programmable logic controller (1-3), data pin (1-3-2), data pin (1-3-4) connects the data input pin (1-6) of center housing (1) respectively, data input pin (1-7), data input pin (1-9), data communication port (1-2-1) end of man-machine interface (1-2) connects data communication port (1-3-5) end of programmable logic controller (1-3), and FPDP (1-3-6) end of programmable logic controller (1-3) connects FPDP (1-1-3) end of variable-frequence governor (1-1).
3, intelligence flocculation administration system according to claim 2 is characterized in that programmable logic controller (1-3) is made up of deviation variation rate computing module (14), obfuscation module (15), performance measurement module (16), manipulated variable correction module (17), control law correcting module (18), fuzzy control rule module (19), fuzzy logic decision module (20), defuzzification module (21), judge module (22), integral control module (23), subtractor (25), multiplier (26); The inner initial control rules of fuzzy control rule module (19) is the historical data of offeing medicine according to manually, the relational database between the raw water flow detected value of the obfuscation of formation, raw water turbidity detected value, turbidity deviation and the flocculant dosage; Port (1-3-5) connects the positive input terminal of subtractor (25), port (1-3-4) connects the negative input end of subtractor (25), the output terminal of subtractor (25) connects the input terminus of deviation variation rate computing module (14), the input terminus (151) of obfuscation module (15), the input terminus (221) of judge module (22), the input terminus (222) of the output terminal connection judgment module (22) of deviation variation rate computing module (14), the input terminus (152) of obfuscation module (15), the input terminus (153) of port (1-3-2) connection mode gelatinization module (15), the input terminus (154) of port (1-3-1) connection mode gelatinization module (15), the input terminus (161) of output terminal (155) the switching performance measurement module (16) of obfuscation module (15), the input terminus (181) of control law correcting module (18), the input terminus (162) of output terminal (156) the switching performance measurement module (16) of obfuscation module (15), the input terminus (191) of fuzzy control rule module (19), the output terminal (157) of obfuscation module (1 5), output terminal (158) connects the input terminus (192) of fuzzy control rule module (19) respectively, input terminus (193), the output terminal (163) of performance measurement module (16) connects the input terminus of manipulated variable correction module (17), the output terminal of manipulated variable correction module (17) connects the input terminus (182) of control law correcting module (18), the output terminal (183) of control law correcting module (18) connects the input terminus (194) of fuzzy control rule module (19), the input terminus of output terminal (195) the connection mode fuzzy logic decision-making module (20) of fuzzy control rule module (19), the output terminal of fuzzy logic decision module (20) connects the input terminus (211) of defuzzification module (21), the output terminal (223) of judge module (22) connects the input terminus of integral control module (23), the output terminal of integral control module (23) connects the input terminus (261) of multiplier (26), the output terminal (212) of defuzzification module (21) connects the input terminus (262) of multiplier (26), output terminal connectivity port (1-3-6) end of multiplier (26).
4, intelligence flocculation administration system according to claim 2, it is characterized in that last the increasing of programmable logic controller (1-3) has intermediate parameters instrument (10), going up to increase at programmable logic controller (1-3) has intermediate parameters controller module (24), totalizer (27), subtractor (28); Go up increase based on the relational database between raw water flow detected value, raw water turbidity detected value, turbidity deviation and the intermediate parameters set(ting)value of obfuscation in fuzzy control rule module (19), its output terminal (213) corresponding to defuzzification module (21), original relational database is corresponding to the output terminal (212) of defuzzification module (21); Intermediate parameters controller (24) adopts conventional proportional integral algorithm, difference according to intermediate parameters set(ting)value and intermediate parameters instrument (10) detected value is carried out the proportional integral computing, and its set(ting)value is revised with the output of integration control module (23) is superimposed automatically by the output terminal (213) of defuzzification module (21); The detection port (10-1) of intermediate parameters instrument (10) connects water outlet (6-3) end of mixing tank (6) and water-in (8-1) end in ligation pond (8), data-in port (1-8) end of data-out port (10-2) the end connection center housing (1) of intermediate parameters instrument (10), the data-in port (1-8) of center housing (1) connect FPDP (1-3-3) end of programmable logic controller (1-3); The output terminal of integral control module (23) connects the input terminus (271) of totalizer (27), the output terminal (213) of defuzzification module (21) connects the input terminus (272) of totalizer (27), the output terminal (273) of totalizer (27) connects the positive input terminal of subtractor (28), FPDP (1-3-3) connects the negative input end of subtractor (28), the output terminal of subtractor (28) connects the input terminus of intermediate parameters controller module (24), the output terminal of intermediate parameters controller module (24) connects the input terminus (262) of multiplier (26), and the output terminal (212) of defuzzification module (21) connects the input terminus (261) of multiplier (26).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410013527 CN1260142C (en) | 2004-01-17 | 2004-01-17 | Intelligent flocculation chemical dosing system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410013527 CN1260142C (en) | 2004-01-17 | 2004-01-17 | Intelligent flocculation chemical dosing system |
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| CN1557737A true CN1557737A (en) | 2004-12-29 |
| CN1260142C CN1260142C (en) | 2006-06-21 |
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| CN 200410013527 Expired - Fee Related CN1260142C (en) | 2004-01-17 | 2004-01-17 | Intelligent flocculation chemical dosing system |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1300014C (en) * | 2005-07-13 | 2007-02-14 | 哈尔滨工业大学 | Method for on-line testing effect of polution removing by permanganate composite drug |
| CN100427175C (en) * | 2005-07-27 | 2008-10-22 | 株式会社日立制作所 | Device and method for controlling infusion of flocculating agent |
| CN102366680A (en) * | 2011-08-23 | 2012-03-07 | 浙江省海洋开发研究院 | Seawater coagulation turbidity removing system |
| CN102531131A (en) * | 2012-02-15 | 2012-07-04 | 泰山医学院 | System and method for controlling adding amount of flocculant |
| CN108502998A (en) * | 2018-03-23 | 2018-09-07 | 湖州新龙潭净水设备有限公司 | A kind of purifier coagulant dosage device |
-
2004
- 2004-01-17 CN CN 200410013527 patent/CN1260142C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1300014C (en) * | 2005-07-13 | 2007-02-14 | 哈尔滨工业大学 | Method for on-line testing effect of polution removing by permanganate composite drug |
| CN100427175C (en) * | 2005-07-27 | 2008-10-22 | 株式会社日立制作所 | Device and method for controlling infusion of flocculating agent |
| CN102366680A (en) * | 2011-08-23 | 2012-03-07 | 浙江省海洋开发研究院 | Seawater coagulation turbidity removing system |
| CN102531131A (en) * | 2012-02-15 | 2012-07-04 | 泰山医学院 | System and method for controlling adding amount of flocculant |
| CN108502998A (en) * | 2018-03-23 | 2018-09-07 | 湖州新龙潭净水设备有限公司 | A kind of purifier coagulant dosage device |
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|---|---|
| CN1260142C (en) | 2006-06-21 |
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