WO2000069780A1 - Process control of the dewatering of sludge - Google Patents
Process control of the dewatering of sludge Download PDFInfo
- Publication number
- WO2000069780A1 WO2000069780A1 PCT/SE2000/000955 SE0000955W WO0069780A1 WO 2000069780 A1 WO2000069780 A1 WO 2000069780A1 SE 0000955 W SE0000955 W SE 0000955W WO 0069780 A1 WO0069780 A1 WO 0069780A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- sludge
- control unit
- content
- thickener
- feeding
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5209—Regulation methods for flocculation or precipitation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
- C02F11/147—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents using organic substances
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
Definitions
- This invention relates generally to sludge thickening processes and in particular concerns a method and a system of controlling such a process.
- Sludge thickening using e.g. drum thickeners or belt thickeners is commonly used in the industry and in municipal sewage treatment and water treatment works.
- a flocculation agent of polymer type is added using a polymer feeding or dosing unit.
- inorganic additions such as metallic salts and calcium hydroxide are used.
- the selection of the flocculant, which is to be added, is often made through manual short time testing, for a certain type of sludge, sludge composition and sludge temperature and with certain other specific process parameters.
- the amount of flocculant/polymer to be added is selected by visually controlling if the filtrate (the water separated at filtration) is reasonably clear or not. A filtrate test can be made, however when the analysis of that test is ready the process conditions may have changed and an adjustment of the polymer addition based on the test result is no longer relevant.
- the amount of dry substance coming out of a thickener, 0 /oDS out is set in a similar way by visually studying thickened sludge. This is often done after the metering or the feeding rate of the polymer has been selected. A sludge test can be taken and corrections can be made, but the test takes a certain time to perform, also here causing the test result to lag behind the changes in process conditions.
- the basic object of the present invention is to eliminate or at least largely reduce the above discussed deficiencies associated with the known technique within the field of sludge thickening.
- the object is to provide a method of improving the efficiency of processes of the kind described above, by optimizing the use of flocculants in the process and thereby minimizing the amount of added flocculant and/or coagulant, while at the same time
- the above stated object is achieved by employing, in the process control, different ways of measuring process parameters on-line, of processing the measured data and, preferably through an iterative control strategy, of changing the process 20 parameters in such a way that the DS-content in the thickened sludge and the flow rate thereof become as desired, so that the consumption of polymers or metallic salts is kept low.
- this object is achieved by controlling the feed rate of the polymer through measurement of the SS content in the filtrate, in order to thereby lower the consumption of the 25 polymer, but above all govern the thickening process in such a way that the DS content of the thickened sludge lies between a highest and a lowest value.
- a system for controlling a process of the kind described above, in accordance with the basic principles of the invention.
- a further aspect of the invention relates to the use of the method and/or system according to the invention for thickening before a digester. Further objects, characteristics and advantages of the invention are clear from the independent patent claims as well as from the following description of exemplifying embodiments.
- Example No. 1 concerning controlling the addition of flocculant with the purpose of minimizing the polvmer consumption at drum thickening or of warning for a flocculant mixture that is no longer active, while at the same time obtaining a DS content in the thickened sludge that lies within a desired range.
- the main object of the invention is to improve the efficiency of thickening processes by optimizing the utilization of flocculants and/or coagulants in the process, thereby minimizing the added amount of flocculants and/or coagulants and at the same time achieving a DS content in the thickened sludge that lies within a desired interval.
- this is achieved in connection with a thickener (1), by providing an optical sensor 14, preferably of infrared type, either applying direct measurement and provided with a cleaning device, or configured in such a way that staining of the sensor units is compensated for, or that changes of the color of the filtrate RF is compensated for.
- the sensor 14 is provided in a specific compartment (not shown) in connection with the pipe 7 carrying the filtrate out from the thickener 1.
- the sensor 14 as well as the opening and closing functions of the compartment and possible associated flushing units are connected to a control unit 2 that is also connected to a feeding pump 3 at units 3, 4 for the addition of flocculants Fi and F 2 , i.e. often polymers.
- the sensor 14 is calibrated considering the specific application and is working in the range of monotonic increased addition of polymer-monotonic decreasing DS content. Two to three limiting conditions are selected, depending upon the measuring conditions.
- the first measuring limit SS max is set equal to the SS content (amount of solids in the filtrate) above which the amount of SS is considered as unacceptable. If the SS content exceeds this value, the control unit 2 increases the feed rate of flocculant Fi until the SS content goes below this value, which is say 400 mg SS/1.
- control unit 2 switches over to the addition of another flocculant F 2 with other flocculation properties.
- the control unit decreases the rate of polymer feed until an SS-value above 100 mg SS/1 has been exceeded.
- the control unit 2 regularly senses the SS content in the filtrate RF and feeds or meters, through an iterative process, in such a way that when the limit value 400 mg SS/1 is reached through a certain polymer feeding, the polymer addition is adjusted down one unit, where the unit size depends upon the actual process conditions.
- the control unit 2 is programmed to sense the SS content at a frequency that is set by the operator.
- the control unit 2 can control the addition of flocculant/polymer based on single measuring points, but preferably changes of the polymer addition are based on mean value calculations based on a number of measuring points.
- hot water can be used as mixing water for the dilution of the concentrated polymer, and said hot water can be controlled to a certain temperature, and can be injected into a flocculant-water mixing vessel 4 through a hot water mixer 5. This increases the normalized time for maturing of the diluted polymer mixture and the resulting effect is lowered polymer consumption.
- the main object of the invention is accomplished, i.e. by measuring the SS content in the filtrate the polymer feed rate can be controlled in such a way that the SS content is kept between a lowest value SS m ⁇ n and a highest value SS max .
- the polymer consumption decreases but above all the thickening process is controlled in such a way that the DS content of the thickened sludge is between a highest and a lowest value.
- Example 2 concerning controlling the polvmer addition to minimize the polvmer consumption, avoiding clogging of the filter cloth and warning for the use of the wrong polvmer or a polymer mixture which is no longer active, in connection with drum thickening, while at the same time other process parameters are automatically changed to minimize the polymer consumption and a changed DS content of the thickened sludge is obtained.
- the automatic control of the polymer addition is supplemented by a continuous iterative search for minima in polymer addition as a function of different process parameters, using the same sensor 14 as in example 1 above.
- Minimization of the flocculant/polymer consumption is made in the same way as in example 1, but is in this case supplemented with an iterative search for polymer addition minima also as a function of other parameters, like e.g. the speed of rotation of the drum.
- the speed V of drum rotation is stepwise lowered from a preselected value, say 10 rpm, with alternating adjustment of the feed rate of polymer addition, and at the same time the SS content in the filtrate RF is measured.
- the control unit 2 can be equipped with a function that governs the temperature of the dilution water in such a way that the polymer addition can be decreased.
- Example 3 concerning control of the DS content within a desired interval while at the same time minimizing the consumption of the flocculant/polymer.
- Results show that even with only a sensor 14 in the filtrate it is possible to control the DS content of the outgoing sludge, DS 0Ut, with reasonable accuracy, so that it is possible to obtain a desired DS content of the thickened sludge FS that is discharged from a thickener 1 through an outlet 8.
- the accuracy of this process increases if the pump for the incoming sludge IS is such that the flow into the thickener 1 is constant, and if the DS content, DS ⁇ n , of incoming sludge is also reasonably constant.
- a desired DS content, DS out can be set in an indirect way, by choosing a certain SS content of the filtrate as set value for the control unit 2, in combination with the selection of other process parameters.
- Example 4 concerning a wav of indirectly, through a multi sensor system, measuring and controlling the outgoing DS content, and at the same time minimizing the polymer addition during drum thickening.
- the optical sensor 14 in the filtrate RF is supplemented with a flow meter 15.
- a sensor 10 for the incoming DS content In the pipe for incoming sludge two sensors are also inserted, a sensor 10 for the incoming DS content and a sensor 11 for the flow.
- the control unit 2 described above can also be connected to the following sensors and functions: i.
- control unit After setting the desired content and flow of DS 0Ut on the control unit 2, the control unit controls and measures according to the following:
- the polymer addition is made according to example 1 above.
- IV. In an iterative process, the DS content DS out is then controlled by stepwise changes of the slope of the drum, the speed of drum rotation and the frequency of spraying. The polymer addition is continuously optimized in a sub-iterative process as described above.
- V. Through an efficient mixing and a continuous measurement of the thickened sludge in the sludge basin before the digester, the DS content in this sludge basin can be used as the main control parameter instead of DS 0U t, and then an adjustment of DS ou t is performed considering the difference between the set value and the actual DS value in the sludge basin. This procedure gives a maximum of efficiency for the following processes like pumping, heat exchanging and digesting in a digester, still minimizing the polymer addition as an important result.
- the thickening process can be controlled in an optimal way, completely auto- matically and without any inspection as well as providing a process economy at its maximum.
- control unit 2 senses that and sets new optimal process parameters.
- the thickening process can be completely automated a) The cost for the addition of polymers can be minimized, which means considerable savings every year and also provides advantages for the environment. b) The cost for the water used for spraying is minimized, which also means large savings. c) The filtrate will on the average become cleaner, which decreases the load on the sewage treatment plant. d) DS out and the flow will be as desired, which gives large advantages for the following process. In the case of a biogas plant this means an increased biogas production and a smaller amount of heated water, and both these two factors considerably improve the economy. In the case that the thickened sludge will be transported, significantly smaller volumes are obtained by using the present invention.
- Example 5 concerning the design of a sludge sensor and the control thereof.
- the sludge content sensor 14 is preferably of the optical type, preferably working in the infrared range, but it is also possible to use e.g. UV-light.
- the sludge sensor can also be of another type, e.g. density sensors or stirrers for sludge basins, sensors for the electrode potential in the case of addition of oxidizing salts, e.g. FeCl 3 or sensors for the conductivity in the case of addition of other salts.
- the infrared sensor consists of two senders/receivers or several pairs thereof, between which the infrared light moves. To avoid staining the senders/receivers are flushed or wiped clean just before the measuring moment, as a part of the measuring process. In the case that more than two senders/receivers are used the color of the water or stains on the interfaces of the senders/receivers can also be compensated for.
- the sensor shall preferably be placed in a specific compartment arranged in such a way, that this compartment can be cleaned by flushing or mechanically, just before the measurement, followed by letting in new filtrate and performing measurements. In this way representative measurement results are obtained when making DS measurements.
- Example 6 concerning a combination of controlling additions of coagulants and of flocculants by sludge thickening.
- the sludge IS can be difficult to thicken also at high polymer additions.
- a sensor 13 can be connected to the control unit for measuring of the charge of the sludge particles before the polymer addition, as well as equipment 12 for the addition of coagulants, in most cases a metallic salt.
- the addition of coagulants is controlled in such a way that either the charge of the sludge particles enters a certain level or the need for polymer addition decreases below a certain level. In this way, the addition of polymer can be decreased.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU49657/00A AU4965700A (en) | 1999-05-14 | 2000-05-14 | Process control of the dewatering of sludge |
EP00931839A EP1196355A1 (en) | 1999-05-14 | 2000-05-14 | Process control of the dewatering of sludge |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9901772A SE9901772D0 (en) | 1999-05-14 | 1999-05-14 | process |
SE9901772-5 | 1999-05-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2000069780A1 true WO2000069780A1 (en) | 2000-11-23 |
Family
ID=20415607
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SE2000/000955 WO2000069780A1 (en) | 1999-05-14 | 2000-05-14 | Process control of the dewatering of sludge |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP1196355A1 (en) |
AU (1) | AU4965700A (en) |
SE (1) | SE9901772D0 (en) |
WO (1) | WO2000069780A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6652757B2 (en) | 2000-05-05 | 2003-11-25 | Black & Veatch Holding Company | Method for high speed dewatering of slurries |
FR2940270A1 (en) * | 2008-12-24 | 2010-06-25 | Degremont | RAPID STATIC DECANTER FOR PRE-THICKENING WATER TREATMENT SLUDGE, AND INSTALLATION COMPRISING SUCH DECANTER. |
US20150052774A1 (en) * | 2013-08-20 | 2015-02-26 | Whirlpool Corporation | Method for drying articles |
WO2018066008A1 (en) * | 2016-10-06 | 2018-04-12 | Lisanti Luciano | System for reducing costs of mechanical dewatering of sludge |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115925067B (en) * | 2022-10-10 | 2023-12-15 | 中建安装集团有限公司 | Mud treatment system and method based on intelligent perception technology |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995033697A1 (en) * | 1994-06-08 | 1995-12-14 | Ab Cdm | Dewatering of suspensions |
DE4442418A1 (en) * | 1994-11-29 | 1996-05-30 | Joachim Friedrich Knauer | Dosing unit for batch addn. of flocculant to aq. sludge from storage |
DE19617528A1 (en) * | 1994-11-29 | 1997-11-13 | Joachim Friedrich Knauer | Apparatus for controlling addition of flocculent to sludge |
WO1998049108A1 (en) * | 1997-04-30 | 1998-11-05 | Ciba Specialty Chemicals Water Treatments Limited | Dewatering of sewage sludge |
-
1999
- 1999-05-14 SE SE9901772A patent/SE9901772D0/en unknown
-
2000
- 2000-05-14 EP EP00931839A patent/EP1196355A1/en not_active Withdrawn
- 2000-05-14 AU AU49657/00A patent/AU4965700A/en not_active Abandoned
- 2000-05-14 WO PCT/SE2000/000955 patent/WO2000069780A1/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995033697A1 (en) * | 1994-06-08 | 1995-12-14 | Ab Cdm | Dewatering of suspensions |
DE4442418A1 (en) * | 1994-11-29 | 1996-05-30 | Joachim Friedrich Knauer | Dosing unit for batch addn. of flocculant to aq. sludge from storage |
DE19617528A1 (en) * | 1994-11-29 | 1997-11-13 | Joachim Friedrich Knauer | Apparatus for controlling addition of flocculent to sludge |
WO1998049108A1 (en) * | 1997-04-30 | 1998-11-05 | Ciba Specialty Chemicals Water Treatments Limited | Dewatering of sewage sludge |
Non-Patent Citations (1)
Title |
---|
JOHN AABO: "Styresystemer reduserer behov for driftstilsyn", TEKNISK UKEBLAD/TEKNIKK, vol. 126, no. 44, 22 October 1979 (1979-10-22), pages 24 - 38, XP002955341 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6652757B2 (en) | 2000-05-05 | 2003-11-25 | Black & Veatch Holding Company | Method for high speed dewatering of slurries |
FR2940270A1 (en) * | 2008-12-24 | 2010-06-25 | Degremont | RAPID STATIC DECANTER FOR PRE-THICKENING WATER TREATMENT SLUDGE, AND INSTALLATION COMPRISING SUCH DECANTER. |
US20150052774A1 (en) * | 2013-08-20 | 2015-02-26 | Whirlpool Corporation | Method for drying articles |
US9194625B2 (en) * | 2013-08-20 | 2015-11-24 | Whirlpool Corporation | Method for drying articles |
WO2018066008A1 (en) * | 2016-10-06 | 2018-04-12 | Lisanti Luciano | System for reducing costs of mechanical dewatering of sludge |
Also Published As
Publication number | Publication date |
---|---|
EP1196355A1 (en) | 2002-04-17 |
AU4965700A (en) | 2000-12-05 |
SE9901772D0 (en) | 1999-05-14 |
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