JPS58128200A - Control device of purifying tank - Google Patents
Control device of purifying tankInfo
- Publication number
- JPS58128200A JPS58128200A JP57010064A JP1006482A JPS58128200A JP S58128200 A JPS58128200 A JP S58128200A JP 57010064 A JP57010064 A JP 57010064A JP 1006482 A JP1006482 A JP 1006482A JP S58128200 A JPS58128200 A JP S58128200A
- Authority
- JP
- Japan
- Prior art keywords
- alkalinity
- washing water
- sludge
- washing
- flow rate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は消化汚泥の洗浄を行う洗浄タンクの制御装置に
係シ、%に消化汚泥のアルカリ度を制御する洗浄タンク
の制御装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a washing tank control device for washing digested sludge, and more particularly, to a washing tank control device for controlling the alkalinity of digested sludge in percent.
下水処理場の汚泥処理プロセスにおいては消化汚泥を脱
水する前に凝集剤を添加する。消化汚泥のアルカリ度は
一般に2000〜3000 mg/z程度と高く、凝集
剤を多量に必要とする。第1図に汚泥のアルカリ度と凝
集剤添加量の変化による脱水機の一過率の変化を示す。In the sludge treatment process at sewage treatment plants, flocculants are added to digested sludge before it is dehydrated. Digested sludge generally has a high alkalinity of about 2000 to 3000 mg/z, and requires a large amount of flocculant. Figure 1 shows changes in the transit rate of the dehydrator due to changes in the alkalinity of the sludge and the amount of flocculant added.
そこで消化汚泥をアルカリ度の低い水で洗浄することに
よシ汚泥のアルカリ度を下げるとともに脱水の障害とな
る圧縮性の高いKかわ状質を洗い流すことによって凝集
剤の節約および脱水機の一過効率の向上を図るために洗
浄プロセスが設けられている。Therefore, by washing the digested sludge with water with low alkalinity, the alkalinity of the sludge is lowered, and the highly compressible K slime, which is an obstacle to dewatering, is washed away, thereby saving on coagulant and making it easier for the dehydrator to pass. A cleaning process is provided to improve efficiency.
従来、消化汚泥を洗浄するための洗浄水量の制御は流入
汚迦量に基づく比率注入制御法が行なわれている。一般
には流入汚泥量に対して4〜5倍の洗浄水量を与えてい
る。しかし、比率注入制御法においては流入汚泥のアル
カリ度が変動すると洗浄汚泥のアルカリ度も変動するこ
とになる。第2図に流入汚泥のアルカリ度が3000m
g/4と2000 mg/lの場合における洗浄水量比
と洗浄汚泥のアルカリ度を示す。九だし洗浄水アルカリ
度はssomg/zである。第2図かられかるように洗
浄水量比を5とした場合、流入汚泥のアルカリ度が20
00 mg/lの時(’I性L 1,1に洗浄汚泥のア
ルカリ度625alt/lであるのに対し、流入汚泥の
アルカリ度が3000 mg/lになる(特性L2)と
洗浄汚泥のアルカリ度は7291ng/lに変化する。Conventionally, the amount of washing water for washing digested sludge has been controlled by a ratio injection control method based on the amount of inflowing sludge. Generally, the amount of washing water is 4 to 5 times the amount of inflowing sludge. However, in the ratio injection control method, when the alkalinity of the inflowing sludge changes, the alkalinity of the washed sludge also changes. Figure 2 shows that the alkalinity of the inflowing sludge is 3000m
The washing water amount ratio and alkalinity of washed sludge in the case of g/4 and 2000 mg/l are shown. The alkalinity of the nine-dashi washing water is ssomg/z. As shown in Figure 2, when the washing water ratio is set to 5, the alkalinity of the inflowing sludge is 20.
When the alkalinity of the washed sludge is 625 alt/l (Characteristic L2), the alkalinity of the washed sludge is 625 alt/l (Characteristic L2). The degree changes to 7291 ng/l.
このアルカリ度の変化は第1図で示した過多凝集剤の添
加量を大きく変えないかぎシ脱水横の一過率が変化する
ことになる。This change in alkalinity results in a change in the transit rate of water dewatering, which does not significantly change the amount of excess flocculant added as shown in FIG.
この為、脱水機の運転管理が難しく、特に脱水機の台数
が多くなる#1ど台数制御が困難になる。For this reason, it is difficult to manage the operation of the dehydrators, and it is especially difficult to control the number of dehydrators in #1, where the number of dehydrators increases.
本発明の目的は脱水機の一過効率を一定にできる洗浄タ
ンクの制御装置を提供することにある。An object of the present invention is to provide a cleaning tank control device that can keep the transient efficiency of a dehydrator constant.
本発明は流入汚泥のアルカリ度と洗浄水のアルカリ度お
よび洗浄水の設定アルカリ度よ)洗浄水量比を求め、こ
の洗浄水量比と流入汚泥量に基づき洗浄水量を制御して
洗浄汚泥のアルカリ度を一定に保つようにしたものであ
る。The present invention calculates the washing water amount ratio (from the alkalinity of the inflowing sludge, the alkalinity of the washing water, and the set alkalinity of the washing water), and controls the washing water amount based on this washing water amount ratio and the amount of inflowing sludge to increase the alkalinity of the washed sludge. is kept constant.
以下、本発明の一実施例を第3図において説明する。な
お、洗浄方式には、1段洗浄方式、2段向流洗浄方式等
があるが、第3図は1段洗浄方式の場合について説明し
てあシ、2段向流洗浄方式の場合も1段洗浄方式と同じ
様に実現出来る。An embodiment of the present invention will be described below with reference to FIG. There are two types of cleaning methods, such as a one-stage cleaning method and a two-stage countercurrent cleaning method. This can be realized in the same way as the stage cleaning method.
第3図において、流入汚泥2は洗浄タンクlに入シ、伊
で述べるようにして加えられる洗浄水5で洗浄される。In FIG. 3, inflowing sludge 2 enters a washing tank l and is washed with washing water 5, which is added as described in FIG.
洗浄タンク1に加えられる洗浄水5は水量調節弁7で調
節される。洗浄された洗浄汚泥lOは脱水機(図示せず
)に加えられ、また、洗浄廃水9は上部から流出する。Washing water 5 added to the washing tank 1 is regulated by a water amount control valve 7. The washed sludge IO is added to a dehydrator (not shown), and the washed wastewater 9 flows out from the top.
流入汚泥2のアルカリ度A−と流量Fb’はアルカリ変
針3および流量計4とで測定される。同様に洗浄水5の
アルカリ度A1と流量F、はアルカリ変針6および流量
計8によって測定される。アルカリ変針3,6および流
量計4,7の測定値は洗浄水演算回路11に加えられる
。洗浄水演算回路11は洗浄汚泥のアルカリ度を設定す
るアルカリ度設定器12゜減算器13,14.除算器1
5.乗算器16および調節計17とから成る。The alkalinity A- and the flow rate Fb' of the inflowing sludge 2 are measured by an alkaline change course 3 and a flow meter 4. Similarly, the alkalinity A1 and the flow rate F of the cleaning water 5 are measured by the alkaline needle 6 and the flow meter 8. The measured values of the alkaline needles 3 and 6 and the flowmeters 4 and 7 are added to the wash water calculation circuit 11. The wash water calculation circuit 11 includes an alkalinity setting device 12° subtractors 13, 14, . Divider 1
5. It consists of a multiplier 16 and a controller 17.
次に動作を説明する。Next, the operation will be explained.
アルカリ変針3で測定した流入汚泥アルカリ度Ahとア
ルカリ置設定値A、差を減算器13で求める。また、ア
ルカリ度設定値A、と洗浄水アルカリ変人、の差を減算
器14で求める。両減算器13.14で求めた差を割算
器15に加え、次式によシ洗浄流量比Rを求める。The difference between the inflow sludge alkalinity Ah measured by the alkaline needle changer 3 and the alkaline setting value A is determined by the subtractor 13. Further, the difference between the alkalinity set value A and the washing water alkalinity is determined by the subtractor 14. The difference determined by both subtracters 13 and 14 is added to the divider 15, and the cleaning flow rate ratio R is determined by the following formula.
h −Am
R冨 □ ・・・・・・(1)aA
−
ただし、Rは洗浄水量比
乗算器16は割算器15で求めた洗浄水量比Rとam計
4で測定した流入汚泥量F−を乗算し、洗浄水量指令F
−を出す、洗浄水量指令F4は調節計17の入力となる
。調節計17は洗浄水量指令F′、と流量計8で測定し
九洗浄水量X、を比較し水量調節弁7の開度を制御する
。p′v>p、の場合は水量調節弁7t−閉方向に操作
し、pL<F、の場合は開方向に操作する。これにょシ
、消化タンク1に加えられる洗浄水5の水量は洗浄汚泥
のアルカリ度が設定値A、となるように制御される。h −Am R wealth □ ・・・・・・(1) aA
- However, R is the washing water amount ratio multiplier 16 which multiplies the washing water amount ratio R obtained by the divider 15 by the inflow sludge amount F- measured by the am meter 4, and the washing water amount command F
The washing water amount command F4 that outputs - becomes an input to the controller 17. The controller 17 compares the washing water amount command F' with the washing water amount X measured by the flow meter 8, and controls the opening degree of the water amount regulating valve 7. When p'v>p, the water flow control valve 7t is operated in the closing direction, and when pL<F, it is operated in the opening direction. At this time, the amount of washing water 5 added to the digestion tank 1 is controlled so that the alkalinity of the washed sludge becomes the set value A.
以上のように、洗浄汚泥のアルカリ度は一定に制御する
ことができる。As described above, the alkalinity of the washed sludge can be controlled to be constant.
以上説明のように本発明によれば、洗浄汚泥のアルカリ
度を一定にできるので、脱水機の一過効率を一定に保つ
ことができる。し九がって、脱水機の運転管理が容易と
なる。As described above, according to the present invention, the alkalinity of the washed sludge can be kept constant, so the transient efficiency of the dehydrator can be kept constant. Therefore, operation management of the dehydrator becomes easier.
第1図は汚泥のアルカリ度と凝集剤添加蓋の変化による
脱水機の濾過効率の変化を示す特性図、第2図は洗浄水
量比と洗浄汚泥に対するアルカリ度の変化を示す特性図
、第3図は本発明の一実施例を示す構成図である。
l・・・洗浄タンク、2・・・流入汚泥、3・・・流入
汚泥アルカリ変針、4・・・流入汚泥置針、5・・・洗
浄水、6・・・洗浄水アルカリ置針、7・・・洗浄水量
調節器、8・・・洗浄水量針、9・・・洗浄廃水、1o
・・・洗浄汚泥、11・・・洗浄水演算回路、12・・
・アルカリ度設定器、13.14・・・減算器、15・
・・除算器、16・・・調節計、・17・・・比較器、
水量調節弁。Figure 1 is a characteristic diagram showing changes in filtration efficiency of the dehydrator due to changes in sludge alkalinity and flocculant addition lid. Figure 2 is a characteristic diagram showing changes in washing water volume ratio and alkalinity to washed sludge. The figure is a configuration diagram showing an embodiment of the present invention. l...Washing tank, 2...Inflow sludge, 3...Inflow sludge alkaline needle change, 4...Inflow sludge placement needle, 5...Washing water, 6...Washing water alkaline placement needle, 7...・Washing water amount regulator, 8...Washing water amount needle, 9...Washing waste water, 1o
...Washing sludge, 11...Washing water calculation circuit, 12...
・Alkalinity setting device, 13.14...Subtractor, 15・
...divider, 16...controller, 17...comparator,
Water flow control valve.
Claims (1)
ク、この洗浄タンクに加える洗浄水量を調節する水量調
節手段、上記流入汚泥と洗浄水のアルカリ度とアルカリ
度設定値によル洗浄水量比を求める手段、上記流入汚泥
流量と洗浄水量によ)洗浄水量指令を出す水量指令手段
、この洗浄水量指令に基づき上記水量調節手段を操作す
る調節針を具備し、洗浄汚泥のアルカリ度を一定値にす
るようにし九洗浄タンクの゛制御装置。1. A washing tank for washing sludge by adding washing water, a water amount adjusting means for adjusting the amount of washing water added to this washing tank, and a washing water amount ratio according to the alkalinity and alkalinity setting value of the above-mentioned inflow sludge and washing water. means for determining the amount of water, a water amount commanding means for issuing a washing water amount command (based on the above-mentioned inflow sludge flow rate and washing water amount), and an adjustment needle for operating the water amount regulating means based on this washing water amount command, so as to maintain the alkalinity of the washed sludge at a constant value. 9. Control device for cleaning tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57010064A JPS58128200A (en) | 1982-01-27 | 1982-01-27 | Control device of purifying tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57010064A JPS58128200A (en) | 1982-01-27 | 1982-01-27 | Control device of purifying tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS58128200A true JPS58128200A (en) | 1983-07-30 |
Family
ID=11739943
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57010064A Pending JPS58128200A (en) | 1982-01-27 | 1982-01-27 | Control device of purifying tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58128200A (en) |
-
1982
- 1982-01-27 JP JP57010064A patent/JPS58128200A/en active Pending
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