CN108776429A - Improve biochemistry pool mixing effect method - Google Patents
Improve biochemistry pool mixing effect method Download PDFInfo
- Publication number
- CN108776429A CN108776429A CN201810633841.4A CN201810633841A CN108776429A CN 108776429 A CN108776429 A CN 108776429A CN 201810633841 A CN201810633841 A CN 201810633841A CN 108776429 A CN108776429 A CN 108776429A
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- China
- Prior art keywords
- biochemistry pool
- impeller
- control unit
- mixing effect
- sludge concentration
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- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 18
- 230000000694 effects Effects 0.000 title claims abstract description 17
- 239000010802 sludge Substances 0.000 claims abstract description 19
- 238000001514 detection method Methods 0.000 claims abstract description 5
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 4
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 4
- 230000005611 electricity Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 230000001737 promoting effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B11/00—Automatic controllers
- G05B11/01—Automatic controllers electric
- G05B11/36—Automatic controllers electric with provision for obtaining particular characteristics, e.g. proportional, integral, differential
- G05B11/42—Automatic controllers electric with provision for obtaining particular characteristics, e.g. proportional, integral, differential for obtaining a characteristic which is both proportional and time-dependent, e.g. P. I., P. I. D.
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- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Automation & Control Theory (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a kind of improvement biochemistry pool mixing effect methods.Step S1:Obtain the sludge concentration steps S2 of biochemistry pool predetermined depth successively according to default detection ordering:Using the sludge concentration of biochemistry pool current depth as the specified rate R (t) of control unit.Step S3:By amount R (t) given herein above and feedback quantity Y (t) synthesis departure E (t).Step S4:By above-mentioned departure E (t) input control unit, and by control unit output controlled quentity controlled variable U (t) is adjusted through PID.Step S5:Above-mentioned controlled quentity controlled variable U (t) is inputted into impeller to control impeller converting operation.Step S6:Counter give the feedback quantity Y (t) that impeller exports to control unit.Improvement biochemistry pool mixing effect method disclosed by the invention, using the sludge concentration of each predetermined depth of biochemistry pool as the input parameter of control system, it adjusts to obtain accurate impeller running frequency by PID closed loops so that impeller is according to above-mentioned running frequency converting operation.
Description
Technical field
The invention belongs to biochemical processing fields, and in particular to a kind of improvement biochemistry pool mixing effect method.
Background technology
Currently, method used in each sewage plant biochemistry pool is impeller power frequency operation, and can not according in biochemistry pool not
Change the running frequency of impeller with the sludge concentration of depth.Therefore, it is impossible to ensure that the sludge in biochemistry pool is uniformly mixed journey
Degree, in fact it could happen that sludge sinks to the bottom lamination.
Invention content
The present invention is directed to the situation of the prior art, overcomes drawbacks described above, provides a kind of improvement biochemistry pool mixing effect method.
The present invention uses following technical scheme, the improvement biochemistry pool mixing effect method to include the following steps:
Step S1:Obtain the sludge concentration of biochemistry pool predetermined depth successively according to default detection ordering;
Step S2:Using the sludge concentration of biochemistry pool current depth as the specified rate R (t) of control unit;
Step S3:By amount R (t) given herein above and feedback quantity Y (t) synthesis departure E (t);
Step S4:By above-mentioned departure E (t) input control unit, and by control unit output controlled quentity controlled variable is adjusted through PID
U(t);
Step S5:Above-mentioned controlled quentity controlled variable U (t) is inputted into impeller to control impeller converting operation;
Step S6:Counter give the feedback quantity Y (t) that impeller exports to control unit.
According to above-mentioned technical proposal, in step S4, controlled quentity controlled variable U (t) is embodied as the running frequency of impeller.
According to above-mentioned technical proposal, described control unit includes proportioner, differentiator and integrator.
Improvement biochemistry pool mixing effect method disclosed by the invention, advantage are, by each pre- depthkeeping of biochemistry pool
Input parameter of the sludge concentration of degree as control system is adjusted to obtain accurate impeller running frequency by PID closed loops, be made
Impeller is obtained according to above-mentioned running frequency converting operation.While promoting in biochemistry pool sludge to be uniformly mixed, it is effectively reduced consumption
Electricity, to reduce the station-service electricity of sewage plant.
Description of the drawings
Fig. 1 is the system block diagram of the preferred embodiment of the present invention.
Reference numeral includes:10- proportioners;20- differentiators;30- integrators;100- impellers.
Specific implementation mode
The invention discloses a kind of improvement biochemistry pool mixing effect methods, with reference to preferred embodiment, to the present invention's
Specific implementation mode is further described.
Referring to Figure 1 of the drawings, Fig. 1 shows the PID control system for improving biochemistry pool mixing effect method.
Preferably, the improvement biochemistry pool mixing effect method includes the following steps:
Step S1:Obtain the sludge concentration of biochemistry pool predetermined depth successively according to default detection ordering;
Step S2:Using the sludge concentration of biochemistry pool current depth as the specified rate R (t) of control unit;
Step S3:By amount R (t) given herein above and feedback quantity Y (t) synthesis departure E (t);
Step S4:By above-mentioned departure E (t) input control unit, and by control unit output controlled quentity controlled variable is adjusted through PID
U(t);
Step S5:Above-mentioned controlled quentity controlled variable U (t) is inputted into impeller 100 to control 100 converting operation of impeller;
Step S6:Control unit is given by feedback quantity Y (t) that impeller 100 exports is counter.
Wherein, in step S4, controlled quentity controlled variable U (t) is embodied as the running frequency of impeller 100.
Wherein, in step S4, described control unit includes proportioner 10, differentiator 20 and integrator 30.
Wherein, after the completion of the corresponding impeller running frequency correction of the sludge deep of biochemistry pool current depth, i.e., according to
Default detection ordering obtains the sludge concentration of the lower depth of biochemistry pool.
According to above preferred embodiment, the preferred embodiment of the present invention is disclosed to improve biochemistry pool mixing effect method, solves
The technical issues of to be existing impeller can not change impeller frequency according to the difference of each depth sludge concentration of biochemistry pool.Change and
Yan Zhi, the preferred embodiment of the present invention is disclosed to improve biochemistry pool mixing effect method, solves the technical solution of above-mentioned technical problem
For:Input parameter of the sludge concentration of each predetermined depth of biochemistry pool as control system, PID arithmetic is carried out by control system,
It obtains accurate impeller running frequency, is transferred to frequency converter, while anti-control system of giving is to calculate departure, from
And control impeller converting operation.Therefore, the preferred embodiment of the present invention is disclosed improves biochemistry pool mixing effect method, acquisition
It has the beneficial effect that, while promoting in biochemistry pool sludge to be uniformly mixed so that the power consumption of impeller is reduced, to reduce sewage
The station-service electricity of factory.
For a person skilled in the art, the technical solution recorded in foregoing embodiments can still be repaiied
Change or equivalent replacement of some of the technical features, all within the spirits and principles of the present invention, made by any repair
Change, equivalent replacement, improvement etc., should be included in protection scope of the present invention.
Claims (3)
1. a kind of improvement biochemistry pool mixing effect method, which is characterized in that include the following steps:
Step S1:Obtain the sludge concentration of biochemistry pool predetermined depth successively according to default detection ordering;
Step S2:Using the sludge concentration of biochemistry pool current depth as the specified rate R (t) of control unit;
Step S3:By amount R (t) given herein above and feedback quantity Y (t) synthesis departure E (t);
Step S4:By above-mentioned departure E (t) input control unit, and by control unit output controlled quentity controlled variable U is adjusted through PID
(t);
Step S5:Above-mentioned controlled quentity controlled variable U (t) is inputted into impeller to control impeller converting operation;
Step S6:Counter give the feedback quantity Y (t) that impeller exports to control unit.
2. improvement biochemistry pool mixing effect method according to claim 1, which is characterized in that in step S4, controlled quentity controlled variable U
(t) it is embodied as the running frequency of impeller.
3. improvement biochemistry pool mixing effect method according to claim 1, which is characterized in that in step S4, the control
Unit includes proportioner, differentiator and integrator.
Priority Applications (1)
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CN201810633841.4A CN108776429A (en) | 2018-06-20 | 2018-06-20 | Improve biochemistry pool mixing effect method |
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CN201810633841.4A CN108776429A (en) | 2018-06-20 | 2018-06-20 | Improve biochemistry pool mixing effect method |
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CN108776429A true CN108776429A (en) | 2018-11-09 |
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CN201810633841.4A Pending CN108776429A (en) | 2018-06-20 | 2018-06-20 | Improve biochemistry pool mixing effect method |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114195255A (en) * | 2021-11-10 | 2022-03-18 | 新余市木林森线路板有限公司 | Method for removing total nitrogen from industrial sewage with high reflux ratio |
Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1285324A (en) * | 2000-09-22 | 2001-02-28 | 北京中环康裕环保工程技术有限公司 | Automatic controller for sewage treatment process |
CN101993151A (en) * | 2009-08-27 | 2011-03-30 | 中国科学院沈阳自动化研究所 | Loop control method for biochemical sewage treatment process |
CN102730831A (en) * | 2012-07-21 | 2012-10-17 | 浙江大学 | Internal circulation hydrolysis anaerobic reaction device |
CN103058457A (en) * | 2012-12-29 | 2013-04-24 | 同济大学苏州研究院 | Device for controlling MBR (Membrane Bio-Reactor) membrane pollution and supplementing aeration and control method of same |
CN203269649U (en) * | 2013-04-25 | 2013-11-06 | 北京铭泽源环境工程有限公司 | Novel automatic biological reaction tank control system for sewage treatment plant |
CN203630652U (en) * | 2013-12-23 | 2014-06-04 | 北京伊普国际水务有限公司 | Control system for reflux quantity of AAO sewage dephosphorization and denitrification process |
CN104150687A (en) * | 2014-07-22 | 2014-11-19 | 河南师范大学 | Sewage treatment automatic control device for reducing production of N2O and operation method of sewage treatment automatic control device |
CN104496016A (en) * | 2014-12-25 | 2015-04-08 | 上海中信水务产业有限公司 | Biochemical oxygenation stirring process and device system |
CN104556372A (en) * | 2013-10-11 | 2015-04-29 | 中国石油化工股份有限公司 | Method for adsorption separation of organic matters by residual sludge |
CN104692611A (en) * | 2015-02-15 | 2015-06-10 | 南京中衡元环保设备有限公司 | Waste catalyst mud water dehydration treatment equipment and waste catalyst mud water dehydration treatment method |
CN105692885A (en) * | 2016-04-22 | 2016-06-22 | 陈建发 | High pollution resistance membrane bioreactor and sewage treatment method |
KR20170034971A (en) * | 2015-09-21 | 2017-03-30 | 김부열 | A device for manufacturing liquid fertilizer contained function of deodorization |
CN107344810A (en) * | 2017-09-04 | 2017-11-14 | 嘉兴奥拓迈讯自动化控制技术有限公司 | Fully-automatic intelligent mud extraction control system |
-
2018
- 2018-06-20 CN CN201810633841.4A patent/CN108776429A/en active Pending
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1285324A (en) * | 2000-09-22 | 2001-02-28 | 北京中环康裕环保工程技术有限公司 | Automatic controller for sewage treatment process |
CN101993151A (en) * | 2009-08-27 | 2011-03-30 | 中国科学院沈阳自动化研究所 | Loop control method for biochemical sewage treatment process |
CN102730831A (en) * | 2012-07-21 | 2012-10-17 | 浙江大学 | Internal circulation hydrolysis anaerobic reaction device |
CN103058457A (en) * | 2012-12-29 | 2013-04-24 | 同济大学苏州研究院 | Device for controlling MBR (Membrane Bio-Reactor) membrane pollution and supplementing aeration and control method of same |
CN203269649U (en) * | 2013-04-25 | 2013-11-06 | 北京铭泽源环境工程有限公司 | Novel automatic biological reaction tank control system for sewage treatment plant |
CN104556372A (en) * | 2013-10-11 | 2015-04-29 | 中国石油化工股份有限公司 | Method for adsorption separation of organic matters by residual sludge |
CN203630652U (en) * | 2013-12-23 | 2014-06-04 | 北京伊普国际水务有限公司 | Control system for reflux quantity of AAO sewage dephosphorization and denitrification process |
CN104150687A (en) * | 2014-07-22 | 2014-11-19 | 河南师范大学 | Sewage treatment automatic control device for reducing production of N2O and operation method of sewage treatment automatic control device |
CN104496016A (en) * | 2014-12-25 | 2015-04-08 | 上海中信水务产业有限公司 | Biochemical oxygenation stirring process and device system |
CN104692611A (en) * | 2015-02-15 | 2015-06-10 | 南京中衡元环保设备有限公司 | Waste catalyst mud water dehydration treatment equipment and waste catalyst mud water dehydration treatment method |
KR20170034971A (en) * | 2015-09-21 | 2017-03-30 | 김부열 | A device for manufacturing liquid fertilizer contained function of deodorization |
CN105692885A (en) * | 2016-04-22 | 2016-06-22 | 陈建发 | High pollution resistance membrane bioreactor and sewage treatment method |
CN107344810A (en) * | 2017-09-04 | 2017-11-14 | 嘉兴奥拓迈讯自动化控制技术有限公司 | Fully-automatic intelligent mud extraction control system |
Non-Patent Citations (1)
Title |
---|
张腾霄,张静: "《新编实用教师百科全书》", 31 July 1992, 中国建材工业出版社 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114195255A (en) * | 2021-11-10 | 2022-03-18 | 新余市木林森线路板有限公司 | Method for removing total nitrogen from industrial sewage with high reflux ratio |
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Application publication date: 20181109 |