JPS5830385A - Purifying device for gas liquor - Google Patents

Purifying device for gas liquor

Info

Publication number
JPS5830385A
JPS5830385A JP12843681A JP12843681A JPS5830385A JP S5830385 A JPS5830385 A JP S5830385A JP 12843681 A JP12843681 A JP 12843681A JP 12843681 A JP12843681 A JP 12843681A JP S5830385 A JPS5830385 A JP S5830385A
Authority
JP
Japan
Prior art keywords
gas liquor
control valve
ammonium water
flow rate
cod value
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
Application number
JP12843681A
Other languages
Japanese (ja)
Inventor
Tomonori Kato
友則 加藤
Ayao Sekikawa
関川 礼夫
Seiji Komura
甲村 省二
Hirohito Ishibashi
石橋 宏仁
Hiroshi Sato
博史 佐藤
Zenkichi Yamanaka
山中 善吉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP12843681A priority Critical patent/JPS5830385A/en
Publication of JPS5830385A publication Critical patent/JPS5830385A/en
Pending legal-status Critical Current

Links

Landscapes

  • Water Treatment By Sorption (AREA)

Abstract

PURPOSE:To purify gas liquor surely and to prolong the life of active carbon by mounting an absorptiometric analyzer to the main flow passage pipe behind the confluent point of the gas liquor passing through a purifying tank contg. active carbon and the gas liquor passing through a flow rate control valve. CONSTITUTION:After the gas liquor produced from a coke furnace is subjected to an activated sludge treatment and a flocculating and settling treatment, the liquor flows into the main flow passage pipe of a purifying device. Part of the gas liquor flows through a bypass flow passage pipe 4 according to the opening and closing of a flow rate control valve 5 and the balance passes through the inside of purifying tanks 3, 3 and is purified by active carbons 2, 2. The COD value contained in the joined gas liquor is detected continuously and automatically with an absorptiometric analyzer 6, and the COD value is controlled to a prescribed value. Namely, when the COD value exceeds a prescribed value, the detection signal is inputted to the valve 5 so that the flow rate of the gas liquor flowing in the pipe 4 is decreased.

Description

【発明の詳細な説明】 本発明は、安水のCOD値を低下させて放流する安水の
浄化処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an ammonium water purification device that reduces the COD value of ammonium water and discharges the ammonium water.

コークス炉から発生する安水には、各種成分及び不純物
が含まれている。安水中の各種成分は、所定の装置によ
り分離回収され、またこれらを分離した安水は、不純物
を含むため活性汚泥処理、凝集沈殿処理した後活性炭で
処理して放流している。しかるに活性炭は、安水を流通
していくと次第にその吸着性能が低下し、活性炭処理し
ても所期の水質が得られjc (なる。このため従来は
、活性炭処理後の放流水のCOD値を定期的(例えば1
日1回)に分析し、その分析値にもとづいて活性炭を取
替えるようにしている。
Ammonium water generated from coke ovens contains various components and impurities. The various components in ammonium water are separated and recovered using predetermined equipment, and since the ammonium water that has been separated contains impurities, it is treated with activated sludge, coagulation and sedimentation, and then treated with activated carbon before being discharged. However, activated carbon's adsorption capacity gradually decreases as it circulates ammonium water, and the desired water quality cannot be obtained even after activated carbon treatment.For this reason, conventionally, the COD value of effluent water after activated carbon treatment was periodically (e.g. 1
The activated carbon is analyzed once a day) and the activated carbon is replaced based on the analyzed value.

この分析法は、111M−マンガン酸カリウム法と称さ
れるもので、分析用の安水に過マンガン酸カリウムの一
定の過刺駿を加え一定時間加熱反応させたのちに消費さ
れた過マンガン酸力11ウムの量から酸素のにを求める
方法である。しかしこの方法は、手分析であるため分析
に手間がかかり、通常1回の分析で2時間、程度かかる
This analytical method is called the 111M-potassium manganate method, in which a certain amount of potassium permanganate is added to ammonium water for analysis, and the permanganate is consumed after a heating reaction for a certain period of time. This is a method to find the amount of oxygen from the amount of force 11 um. However, this method is time-consuming because it is a manual analysis, and one analysis usually takes about two hours.

しかも1日1回の分析で活性炭の取替時期を判定する場
合、分析間隔が長いため安全性を十分考慮して目標値よ
りもかなり低い値で取替える必要がある。また活性炭は
、使用初期には吸着性能が大きいため短期間で吸着性能
が劣化する。このため活性炭の取替頻度が多くなる。
Furthermore, when determining when to replace activated carbon by analyzing it once a day, the analysis interval is long, so it is necessary to fully consider safety and replace the activated carbon at a value considerably lower than the target value. In addition, activated carbon has a high adsorption performance in the initial stage of use, so the adsorption performance deteriorates in a short period of time. For this reason, activated carbon must be replaced more frequently.

本発明は、上記事情に鑑みてなされたもので、その目的
きするところはCOD値を連続かつ自す1的に検出して
分析にかける手間を省く七ともに安水の浄化を確実にお
こなえ、しかも活性炭の寿命を長くしてその取替周期を
長くすることができる安水の浄化処理装置を得んとする
ものである。
The present invention has been made in view of the above circumstances, and its purpose is to continuously and automatically detect the COD value and eliminate the trouble of analyzing it, as well as to reliably purify cheap water. Moreover, it is an object of the present invention to provide an ammonium water purification device that can prolong the life of activated carbon and extend its replacement cycle.

すなわち本発明は、活性炭入り浄化槽を装着した安水の
主流路管に、流量制御弁を取付けたバイパス流路管を並
列に配設し、かつ浄化槽を通る安水と流量制御弁を通る
安水との合流点以降の主流路管に、安水中のCOD値を
検出する吸光度分析計を取付け、該分析計の検出信号に
もさづいて流量制御弁を開閉動作するようにしたことを
特徴とする安水の浄化処理装置である。
That is, the present invention provides a main flow pipe for ammonium water equipped with an activated carbon-containing septic tank, and a bypass flow pipe equipped with a flow rate control valve arranged in parallel. An absorbance analyzer for detecting the COD value in the ammonium chloride solution is attached to the main flow pipe after the confluence point with the water, and the flow control valve is opened and closed based on the detection signal of the analyzer. This is a purification device for ammonium water.

以下本発明を図示する実施例を参照して説明する。The present invention will be described below with reference to illustrative embodiments.

第1図は安水の浄化処理装置の系統図である。FIG. 1 is a system diagram of the ammonium water purification equipment.

この浄化処理装置は、安水の流通する主流路管Iに活性
炭2を入れた浄化槽3を装着し、この〜主流路管Iに対
してバイパス流路管4を並列に配設している。このバイ
パス流路管4には、電′磁弁等の流量制御弁5が装着さ
れている。す(に主流路管J[7才、浄化槽3,3を通
る安水と流量制御弁5を通る安水吉の合流点以降Qで吸
光度分析計6を取付けている。この吸光度分析計6は、
安水の吸光度により安水中のCOD値を検出するもので
、この検出信号にもとづいてθ1し量制御弁5を開閉動
作するものである。この吸光度分析計6は、低圧水銀灯
からなる光源7古光電累子8,8との間に吸収セル9(
+−紫外線フィルタ10及び可視フィルタ11を配置し
、光′iにも素子8.8からの電気信号を可視/紮外選
別増幅器12、対数増幅器X3に通して指示i1’ 1
4に表示するものである。なお図中15は制御部。
In this purification treatment apparatus, a septic tank 3 containing activated carbon 2 is attached to a main flow pipe I through which ammonium chloride flows, and a bypass flow pipe 4 is arranged in parallel to the main flow pipe I. A flow control valve 5 such as an electromagnetic valve is attached to the bypass flow path pipe 4. The absorbance analyzer 6 is installed in the main flow pipe J [7 years old, Q after the confluence of the ammonium water that passes through the septic tanks 3 and 3 and the ansuzu-kichi that passes through the flow rate control valve 5. This absorbance analyzer 6 ,
The COD value in the ammonium water is detected based on the absorbance of the ammonium water, and the amount control valve 5 is opened and closed at θ1 based on this detection signal. This absorbance analyzer 6 has an absorption cell 9 (
A +- ultraviolet filter 10 and a visible filter 11 are arranged, and the electric signal from the element 8.8 is passed through the visible/external selection amplifier 12 and the logarithmic amplifier X3 to direct the light i1'1.
4. Note that 15 in the figure is a control section.

16は自動洗浄バラ・チ測定制御回路、17は光源制御
回路、18は同期回路、19は同期モータ、20はピス
トンモータである。
Reference numeral 16 designates an automatic cleaning variation measurement control circuit, 17 a light source control circuit, 18 a synchronous circuit, 19 a synchronous motor, and 20 a piston motor.

この吸光度分析計6は、直接COD値を測定するもので
はないが、この吸光度分析計6の分析結果と手分析によ
る分析結果とを比較すると第3図に示すように直線的な
関係となる。従ってこの分析計6による分析は、信頼性
があるといえる。
Although this absorbance analyzer 6 does not directly measure the COD value, when the analysis results of this absorbance analyzer 6 are compared with the results of manual analysis, a linear relationship is obtained as shown in FIG. 3. Therefore, it can be said that the analysis by this analyzer 6 is reliable.

次にこのように構成された浄化処理装置の作用5:説明
する。
Next, operation 5 of the purification treatment apparatus configured as described above will be explained.

コークス炉から発生した安水は、活性汚泥処理、凝集沈
殿処理した後、浄化処理装置の主流路管Iに流入する。
The ammonium water generated from the coke oven is subjected to activated sludge treatment and coagulation sedimentation treatment, and then flows into the main flow pipe I of the purification treatment equipment.

ここに流入した安水の一部は、流量制御弁5の開閉に応
じてバイパス流路管4に流れ、残りは浄化槽3.3内を
通って活性炭2.2により浄化される。浄化された安水
とバイパス流路管4を流れた未浄化の安水とは合流して
一旦処理水[22に入り、この後放流される。
A part of the ammonium water that has flowed here flows into the bypass channel pipe 4 according to the opening and closing of the flow rate control valve 5, and the rest passes through the septic tank 3.3 and is purified by the activated carbon 2.2. The purified ammonium water and the unpurified ammonium water flowing through the bypass flow path pipe 4 join together and enter the treated water [22], after which they are discharged.

しかして本発明では、合流後の安水中に含まれるCOD
値を吸光度分析計4で連続かつ自動的に検知して、CO
D値が所定の値となるようにする。すなわちCOD値が
所定の値を越える場合には、検知信号を流・量制御弁5
に入力してバイパス流路管4を流れる安水の流量が少な
くなるように動作させる。またCOD値が所定の値より
も低い場合には、流量制御弁4を作動してバイパス流蛮
管4を流れる安水の流u1が多くなるようにする。
However, in the present invention, COD contained in ammonium water after merging
The CO value is continuously and automatically detected by the absorbance analyzer 4.
The D value is set to a predetermined value. In other words, if the COD value exceeds a predetermined value, the detection signal is sent to the flow/volume control valve 5.
is input so that the flow rate of ammonium water flowing through the bypass flow path pipe 4 is reduced. Further, when the COD value is lower than a predetermined value, the flow control valve 4 is operated to increase the flow u1 of ammonium water flowing through the bypass flow pipe 4.

このように本発明によれば活性炭2の吸着性能が高いさ
きにはここに少量の安水を流し、吸着性能が低くなるに
従ってここに流れる安水の量を多くして常に安水全体が
所定の値になるようにしている。このため活性炭の吸着
性能の低下度合が少rc <活性炭を長寿命とするとと
もに活性炭の取替周期を長くすることができる。またC
OD値を自動的に検出し−Cいるので従来のように分析
に時間と労力を要することがない。
As described above, according to the present invention, when the adsorption performance of the activated carbon 2 is high, a small amount of ammonium water is poured here, and as the adsorption performance becomes low, the amount of ammonium water flowing here is increased so that the entire ammonium water is always kept at a predetermined level. The value is set to . Therefore, the degree of deterioration of the adsorption performance of the activated carbon is small.It is possible to make the activated carbon have a long life and to lengthen the replacement cycle of the activated carbon. Also C
Since the OD value is automatically detected and calculated, the time and labor required for analysis is not required as in the conventional method.

またCOD値を連続的に常時監視しているので。Also, COD values are continuously monitored at all times.

放流水の浄化を確実におこなうことができる。Effluent water can be purified reliably.

次に本発明の実施例につき説明する。Next, examples of the present invention will be described.

第1図に示す浄化装置において、活性汚泥処理、凝集沈
殿処理をおこなった安水を流し、その流面、バイパス流
路管に流れる流量及びCOD値をそれぞれ測定した。そ
の結果を第4図に示す。
In the purification apparatus shown in FIG. 1, ammonium water subjected to activated sludge treatment and coagulation and sedimentation treatment was flowed, and the flow surface, the flow rate flowing into the bypass flow pipe, and the COD value were measured. The results are shown in FIG.

第4図から明らかなように安水中のCOD値を所宇の値
に保持でき、又活性炭の取替時期が23日に延長された
As is clear from Figure 4, the COD value in the ammonium water was maintained at the desired value, and the replacement period for activated carbon was extended to 23 days.

一方従来の方法で処理した場合、活性炭の取替時期が1
0日と短かかった。
On the other hand, when treated with the conventional method, the activated carbon replacement period is 1
It took only 0 days.

以」−の如く本発明によれば、吸光度分析計の検知信号
てもとづいてCOD値を一定に保持するようにしたので
処理の自動化を図り作業性が向上するとさもに活性炭の
取替周期を長くしてう〕/ニソグコストを低くすること
ができる顕著な効果を奏する。
As described above, according to the present invention, the COD value is maintained constant based on the detection signal of the absorbance analyzer, thereby automating the process, improving work efficiency, and lengthening the replacement cycle of activated carbon. ]/This has the remarkable effect of lowering costs.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は安水の浄化処理装置の一例を示す系統図、第2
図は同装置に取付ける吸光度分析計の原理図、第3図は
同吸光度分析計の特性を示す図、第4図は、第1図の浄
化処理装置を用いた実施例におけるCOD値及びバイパ
ス流路管に流れる安水流量の経時的変化を示す図である
。 I・・・主流路管、2・・・活性炭、3・・・浄化槽、
4・・・バイパス流路管、5・・・流量制御弁、6・・
・吸光度分析計。
Figure 1 is a system diagram showing an example of a cheap water purification equipment;
Figure 3 shows the principle of the absorbance analyzer attached to the same device, Figure 3 shows the characteristics of the absorbance analyzer, and Figure 4 shows the COD value and bypass flow in an example using the purification equipment shown in Figure 1. It is a figure which shows the change with time of the ammonium water flow volume which flows into a pipe. I...Main flow pipe, 2...Activated carbon, 3...Septic tank,
4... Bypass flow path pipe, 5... Flow rate control valve, 6...
・Absorbance analyzer.

Claims (1)

【特許請求の範囲】[Claims] 活性炭入り浄化槽を装着した安水の主流路管に、流量制
御弁を取付けたバイパス流路管を並列に配設し、かつ浄
化槽を通る安水と流量制御弁を通る安水、肚の合流点以
降の主流路管に、安水中のCOD値を検出する吸光度分
析計を取付け、該分析計の検出信号にもとづいて流量制
御弁を開閉+fd)作するようにしたことを特徴とする
安水の浄化処理装置。
A bypass flow pipe equipped with a flow control valve is arranged in parallel to the main flow pipe of ammonium water equipped with an activated carbon-containing septic tank, and the junction of ammonium water passing through the septic tank, ammonium water passing through the flow rate control valve, and Nai is created. An absorbance analyzer for detecting the COD value in the ammonium water is attached to the subsequent main flow pipe, and a flow control valve is opened and closed based on the detection signal of the analyzer. Purification treatment equipment.
JP12843681A 1981-08-17 1981-08-17 Purifying device for gas liquor Pending JPS5830385A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12843681A JPS5830385A (en) 1981-08-17 1981-08-17 Purifying device for gas liquor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12843681A JPS5830385A (en) 1981-08-17 1981-08-17 Purifying device for gas liquor

Publications (1)

Publication Number Publication Date
JPS5830385A true JPS5830385A (en) 1983-02-22

Family

ID=14984690

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12843681A Pending JPS5830385A (en) 1981-08-17 1981-08-17 Purifying device for gas liquor

Country Status (1)

Country Link
JP (1) JPS5830385A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61279663A (en) * 1985-06-04 1986-12-10 Sumitomo Electric Ind Ltd Production of composite metallic material
JPH032362A (en) * 1989-05-29 1991-01-08 Nippon Steel Corp Thermally sprayed roll for steel material treatment and its production
JPH04335998A (en) * 1991-05-13 1992-11-24 Hitachi Zosen Corp Coal burning boiler tube

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61279663A (en) * 1985-06-04 1986-12-10 Sumitomo Electric Ind Ltd Production of composite metallic material
JPH032362A (en) * 1989-05-29 1991-01-08 Nippon Steel Corp Thermally sprayed roll for steel material treatment and its production
JPH0564706B2 (en) * 1989-05-29 1993-09-16 Shinnippon Seitetsu Kk
JPH04335998A (en) * 1991-05-13 1992-11-24 Hitachi Zosen Corp Coal burning boiler tube

Similar Documents

Publication Publication Date Title
KR20230112157A (en) The water treatment management device and water quality monitoring method
KR950701427A (en) Method and Apparatus for Predicting End-of-Life of a Consumable in a Fluid Purification System
JPS5833037B2 (en) Activated sludge wastewater purification method and equipment
JPS5830385A (en) Purifying device for gas liquor
SE503918C2 (en) Apparatus for purifying water comprising a pressurized membrane chamber and a method for determining the flushing time of a pressurized membrane chamber
KR102087642B1 (en) Total organic carbon measuring instrument automates sample and gas supply.
CN104297197A (en) Water pollution collection device and method
CN113551708B (en) Water balance evaluation and control method for wet flue gas desulfurization system of thermal power plant
JP4744289B2 (en) Water quality measuring device
JP2005313022A (en) Raw water quality estimating device
JP4466046B2 (en) Approximate BOD5 measurement method, approximate BOD5 measurement apparatus, water quality monitoring apparatus and wastewater treatment system using this apparatus
Häck et al. Online load measurement in combined sewer systems–possibilities of an integrated management of waste water transportation and treatment
JP2002177944A (en) Treatment equipment for waste ammonium ion measure liquid and ammonium ion measuring instrument having the same
JPH08136526A (en) Continuous measuring apparatus for concentration of dissolved ozone
CN214309790U (en) Water sample pretreatment system for high turbid water analysis instrument
JP3223726B2 (en) Method and apparatus for measuring ultraviolet absorbance for process
DK179159B1 (en) An appartus for treating raw water
CN208705102U (en) Coal gasification waste water sampling line with choke preventing function
JP2829050B2 (en) Water treatment equipment
JP2020085779A (en) Ion concentration measurement method and device in discharge water
JP4153893B2 (en) Water treatment method and water treatment system
CN215640849U (en) Online chloride ion automatic measuring device of desulfurization slurry
SU812753A1 (en) Automatic device for control of waste and natural water purification processes
JP2000088718A (en) Method for pretreating sample gas for gas analyzer
SU1076642A1 (en) Method of quality control of compressor passage section cleaning