JP2003266061A - Treatment method for waste water in water-bearing gas holder and apparatus therefor - Google Patents

Treatment method for waste water in water-bearing gas holder and apparatus therefor

Info

Publication number
JP2003266061A
JP2003266061A JP2002073421A JP2002073421A JP2003266061A JP 2003266061 A JP2003266061 A JP 2003266061A JP 2002073421 A JP2002073421 A JP 2002073421A JP 2002073421 A JP2002073421 A JP 2002073421A JP 2003266061 A JP2003266061 A JP 2003266061A
Authority
JP
Japan
Prior art keywords
water
wastewater
gas holder
tank
containing gas
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
JP2002073421A
Other languages
Japanese (ja)
Inventor
Hitoshi Rokutanda
等 六反田
Hideo Takeuchi
秀雄 竹内
Hideki Morimoto
秀樹 森本
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.)
SHITO SURBLAST Ltd
Sintokogio Ltd
Original Assignee
SHITO SURBLAST Ltd
Sintokogio 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 SHITO SURBLAST Ltd, Sintokogio Ltd filed Critical SHITO SURBLAST Ltd
Priority to JP2002073421A priority Critical patent/JP2003266061A/en
Publication of JP2003266061A publication Critical patent/JP2003266061A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Removal Of Floating Material (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a treatment method for waste water in a water-bearing gas holder which can reduce the treatment cost including the transportation cost and shorten the treatment time, and an apparatus therefor. <P>SOLUTION: The waste water treatment method comprises a process for supplying water and oil stored in the water-bearing gas holder as primary waste water to a raw water tank by an extraction pump, a process for floating the oil contained in the primary waste water in the raw water tank to be removed by a floating oil remover and then making the residual water flow into a control tank as secondary waste water, a process for discharging the secondary waste water in the control tank to a filter by a drainage pump and filtering it while sticking suspended solids therein to the inside of the filter, and a process for releasing the water after filtration as filtered water. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、有水ガスホルダ内
の廃水処理方法及びその装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for treating waste water in a water gas holder.

【0002】[0002]

【従来の技術】現在、整圧所において、使用していない
ガスホルダの内部には、錆の発生を防止するために水と
油が注入されている。この水と油は、ガスホルダを解体
廃棄する場合又は再使用する場合に抜き取るが、従来は
抜き取ってタンクロ−リ−車で遠方の廃水処理場まで運
んで所定の廃水処理が成されていた。そのため、輸送費
を含めた処理費用が高く、かつ処理時間も長くかかると
いう問題があった。
2. Description of the Related Art At present, in a pressure regulating station, water and oil are injected into an unused gas holder in order to prevent rusting. The water and oil are extracted when the gas holder is dismantled and discarded or reused. In the past, the water and oil were extracted and transported to a distant wastewater treatment plant by a tank truck to perform predetermined wastewater treatment. Therefore, there is a problem that the processing cost including the transportation cost is high and the processing time is long.

【0003】[0003]

【発明が解決しようとする課題】本発明は上記の問題に
鑑みて成されたもので、輸送費を含めた処理費用を安価
にすることができると共に処理時間を短縮することがで
きる有水ガスホルダ内の廃水処理方法及びその装置を提
供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and can reduce the processing cost including the transportation cost and reduce the processing time. It is an object of the present invention to provide a wastewater treatment method and apparatus therefor.

【0004】[0004]

【課題を解決するための手段】上記の目的を達成するた
めに本発明における有水ガスホルダ内の廃水処理方法
は、有水ガスホルダ内に溜められた水と油を一次廃水と
して抜出ポンプで原水タンクに送り込む工程と、該原水
タンク内の前記一次廃水に含まれる油を浮上させて浮上
油除去装置で除去した後、残りの水を二次廃水として制
御タンクへ流入させる工程と、該制御タンク内の前記二
次廃水を排水ポンプで濾過フィルタへ排水して該二次廃
水中の浮遊物質を濾過フィルタ内に付着させて該二次廃
水を濾過する工程と、該濾過後の水を濾過水として放流
する工程と、を有することを特徴とする。
In order to achieve the above object, a method for treating wastewater in a water-containing gas holder according to the present invention is a method in which water and oil accumulated in the water-containing gas holder are extracted as primary wastewater by a raw water pump. A step of sending it to a tank, a step of levitating the oil contained in the primary waste water in the raw water tank and removing it with a floating oil removing device, and then flowing the remaining water into the control tank as secondary waste water; A step of draining the secondary waste water in a secondary filter into a filtration filter with a drainage pump, depositing suspended matter in the secondary waste water inside the filter to filter the secondary waste water, and filtering the secondary filtered water. And a step of discharging the product.

【0005】また本発明における有水ガスホルダ内の廃
水処理方法は、前記制御タンクに流入される二次廃水の
水量に応じて前記抜出ポンプ及び排水ポンプの運転を制
御することを特徴とする。
The method for treating wastewater in the water-containing gas holder according to the present invention is characterized in that the operation of the extraction pump and the drainage pump is controlled according to the amount of secondary wastewater flowing into the control tank.

【0006】さらに本発明における有水ガスホルダ内の
廃水処理方法は、前記原水タンク内の一次廃水又は前記
制御タンク内の二次廃水に凝集剤を添加して該一次廃水
中又は該二次廃水中の浮遊物質を凝集させることを特徴
とする。
Further, in the wastewater treatment method in the water-containing gas holder according to the present invention, a coagulant is added to the primary wastewater in the raw water tank or the secondary wastewater in the control tank to add the primary wastewater or the secondary wastewater. It is characterized by aggregating the suspended solids.

【0007】さらに本発明における有水ガスホルダ内の
廃水処理方法は、前記濾過フィルタ内に付着した浮遊物
質を該濾過フィルタから取り出して洗浄した後、脱水機
により脱水することを特徴とする。
Further, the method for treating waste water in the water-containing gas holder according to the present invention is characterized in that the floating substances adhering to the inside of the filtration filter are taken out from the filtration filter, washed, and then dehydrated by a dehydrator.

【0008】また上記の目的を達成するために本発明に
おける有水ガスホルダ内の廃水処理装置は、有水ガスホ
ルダ内から抜出ポンプを介して抜き出された水と油を一
次廃水として貯蔵する原水タンクと、該原水タンクに付
設されて、前記一次廃水から浮上する油を除去する浮上
油除去装置と、前記原水タンクから流出される浮上油除
去後の水を二次廃水として貯蔵する制御タンクと、該制
御タンクから排水ポンプを介して排水された前記二次廃
水中の浮遊物質が付着されて該二次廃水を濾過する濾過
フィルタと、を具備することを特徴とする。
In order to achieve the above object, the waste water treatment apparatus in the water-containing gas holder according to the present invention is a raw water for storing water and oil extracted from the water-containing gas holder via a discharge pump as primary waste water. A tank, a floating oil removing device attached to the raw water tank for removing floating oil from the primary wastewater, and a control tank for storing water after floating oil removal flowing out of the raw water tank as secondary wastewater And a filtration filter to which the suspended matter in the secondary wastewater discharged from the control tank through a drainage pump is attached to filter the secondary wastewater.

【0009】また本発明における有水ガスホルダ内の廃
水処理装置は、前記制御タンクに前記二次廃水の水量を
5段階に検知するレベル計を設置し、最上限では廃水処
理装置全体を停止させ、上限では前記抜出ポンプを停止
させ、第1下限では抜出ポンプを運転させ、第2下限では
前記排水ポンプを運転させ、最下限では排水ポンプを停
止させるようにしたことを特徴とする。
In the wastewater treatment device in the water-containing gas holder according to the present invention, a level meter for detecting the amount of the secondary wastewater in five levels is installed in the control tank, and the wastewater treatment device as a whole is stopped at the upper limit. The extraction pump is stopped at the upper limit, the extraction pump is operated at the first lower limit, the drainage pump is operated at the second lower limit, and the drainage pump is stopped at the lowest limit.

【0010】さらに本発明における有水ガスホルダ内の
廃水処理装置は、前記原水タンク又は制御タンクに凝集
剤滴下装置を付設することを特徴とする。
Further, the waste water treatment device in the water-containing gas holder according to the present invention is characterized in that a coagulant dropping device is attached to the raw water tank or the control tank.

【0011】さらに本発明における有水ガスホルダ内の
廃水処理装置は、前記濾過フィルタに、その内圧を検知
する圧力センサを取り付けたことを特徴とする。
Further, the wastewater treatment apparatus in the water-containing gas holder according to the present invention is characterized in that a pressure sensor for detecting the internal pressure of the filtration filter is attached to the filtration filter.

【0012】さらに本発明における有水ガスホルダ内の
廃水処理装置は、前記濾過フィルタから取り出されて洗
浄された浮遊物質を脱水する脱水機を具備することを特
徴とする。
Further, the wastewater treatment apparatus in the water-containing gas holder according to the present invention is characterized by comprising a dehydrator for dehydrating the suspended matter taken out from the filtration filter and washed.

【0013】[0013]

【作用】有水ガスホルダの解体廃棄又は再使用に際し、
本発明の廃水処理装置を搬入、仮設して有水ガスホルダ
内の水と油を抜き出して処理を行うことによって、処理
済水は下水あるいは河川にそのまま放流でき、浮遊物質
のみを産業廃棄物として処分すればよく、従来に比べて
輸送費を含めた処理費用を大幅に削減できると共に処理
時間を大幅に短縮できる。
[Operation] When dismantling, discarding or reusing the water gas holder,
By carrying in the wastewater treatment device of the present invention, temporarily installing it, and extracting water and oil from the water gas holder to perform treatment, the treated water can be discharged as it is to sewage or a river, and only suspended substances are disposed as industrial waste. As a result, the processing cost including the transportation cost can be significantly reduced and the processing time can be significantly reduced as compared with the conventional method.

【0014】[0014]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて詳しく説明する。図1において、左寄り位置
には有水ガスホルダ1が配備されている。該有水ガスホ
ルダ1内には水と油が注入されていて、底部には沈降し
た汚泥1Aが、その上部には水1Bが、さらに水1Bの
上部には浮上した油1Cがそれぞれ層状になって貯蔵さ
れている。そして、前記有水ガスホルダ1の右外側には
廃水処理装置Mが搬入、仮設されている。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the drawings. In FIG. 1, a water-containing gas holder 1 is arranged at the left side position. Water and oil are injected into the water-containing gas holder 1, and the sludge 1A that has settled at the bottom, the water 1B at the upper part, and the floating oil 1C at the upper part of the water 1B are layered. Stored. Then, a wastewater treatment device M is carried in and temporarily installed on the outer right side of the water-containing gas holder 1.

【0015】次に廃水処理装置Mについて説明する。有
水ガスホルダ1のすぐ右外側には有水ガスホルダ1内か
ら抜出ポンプ2を介して抜き出された水1Bと油1Cを
一次廃水として貯蔵する原水タンク3が配置され、該原
水タンク3上方には、前記一次廃水から浮上する油1C
を除去する浮上油除去装置4が付設されていると共に前
記一次廃水中の浮遊物質を凝集させる凝集剤を該一次廃
水に添加する凝集剤滴下装置5が付設されている。
Next, the wastewater treatment device M will be described. Immediately outside the wet gas holder 1 is a raw water tank 3 for storing water 1B and oil 1C extracted from the wet gas holder 1 via a discharge pump 2 as primary waste water, and above the raw water tank 3. 1C of oil floating from the primary wastewater
A flotation oil removing device 4 for removing the coagulant and a flocculant dropping device 5 for adding a coagulant for coagulating the suspended solids in the primary wastewater to the primary wastewater are attached.

【0016】また原水タンク3の下流には原水タンク3
から流出される浮上油除去後の水を二次廃水として貯蔵
する制御タンク6が配置されている。該制御タンク6に
は図2に示すように、前記二次廃水の水量を5段階に検
知するレベル計9が設置されており、最上限をa、上限
をb、第1下限をc、第2下限をd、最下限をeとしてい
る。
The raw water tank 3 is located downstream of the raw water tank 3.
A control tank 6 is arranged for storing the water after the floating oil removed from the tank is stored as secondary waste water. As shown in FIG. 2, the control tank 6 is provided with a level meter 9 for detecting the amount of the secondary wastewater in five stages, with the upper limit being a, the upper limit being b, the first lower limit being c, and the first lower limit being c. 2 The lower limit is d and the lower limit is e.

【0017】そして、該制御タンク6の下流には制御タ
ンク6から排水ポンプ8を介して排水された前記二次廃水
中の浮遊物質が付着されて該二次廃水を濾過する濾過フ
ィルタ7A、7Bが配置されており、該濾過フィルタ7
A、7Bには、その内圧を検知する圧力センサ10A、10
Bが取り付けられている。また濾過フィルタ7A、7Bの
真上には前記二次廃水の流路を開閉する開閉弁11A、11
Bが取り付けられている。
Then, downstream of the control tank 6, suspended substances in the secondary wastewater drained from the control tank 6 through the drainage pump 8 are attached to filter the secondary wastewater by filtration filters 7A, 7B. Is disposed, and the filtration filter 7
A and 7B have pressure sensors 10A and 10B for detecting their internal pressures.
B is attached. On-off valves 11A and 11 for opening and closing the flow path of the secondary waste water are provided directly above the filtration filters 7A and 7B.
B is attached.

【0018】さらに前記濾過フィルタ7A、7Bの下流に
は該濾過フィルタ7A、7Bから取り出された前記二次廃
水中の浮遊物質を洗浄する洗浄槽12が配置され、該洗浄
槽12の下流には洗浄された浮遊物質を脱水する脱水機と
しての真空濾過機13が配置されている。
Further, a washing tank 12 for washing suspended substances in the secondary waste water taken out from the filtration filters 7A, 7B is arranged downstream of the filtration filters 7A, 7B, and downstream of the washing tank 12. A vacuum filter 13 as a dehydrator for dehydrating the washed suspended matter is arranged.

【0019】このように構成されたものは、まず、有水
ガスホルダ1内に溜められた水1Bと油1Cを一次廃水と
して抜出ポンプ2で原水タンク3に送り込む。次に原水タ
ンク3内の前記一次廃水を所定時間放置して該一次廃水
に含まれる油1Cを浮上させた後、浮上した油1Cを浮上
油除去装置4で除去する。さらに凝集剤滴下装置5で前
記原水タンク3内の一次廃水に凝集剤を添加して該一次
廃水中の浮遊物質を凝集させる。ここで、浮遊物質と
は、例えば鉄分などのことをいい、鉄分の場合の凝集剤
としては、石灰、ポリ塩化アルミニウム等が挙げられ
る。
In the thus constructed apparatus, first, the water 1B and the oil 1C stored in the water-containing gas holder 1 are sent to the raw water tank 3 by the extraction pump 2 as primary waste water. Next, the primary wastewater in the raw water tank 3 is left for a predetermined time to float the oil 1C contained in the primary wastewater, and then the floating oil 1C is removed by the floating oil removing device 4. Further, the flocculant dropping device 5 adds a flocculant to the primary wastewater in the raw water tank 3 to flocculate suspended solids in the primary wastewater. Here, the suspended matter refers to, for example, iron, and examples of the aggregating agent in the case of iron include lime, polyaluminum chloride, and the like.

【0020】次に原水タンク3で上述の処理をされた水
を二次廃水として制御タンク6へ流入させる。制御タン
ク6では流入される二次廃水の水量を前記レベル計9に
より検知し、該水量に応じて前記抜出ポンプ2及び排水
ポンプ8の運転を制御する。具体的には、上述したよう
に水量を5段階に検知し、前記最上限aでは廃水処理装
置M全体を停止させ、上限bでは前記抜出ポンプ2を停
止させ、第1下限cでは抜出ポンプ2を運転させ、第2下
限dでは前記排水ポンプ8を運転させ、最下限eでは排
水ポンプ8を停止させることにより、制御タンク6内の水
量を過不足なく常時適量に保つようにする。
Next, the water treated as described above in the raw water tank 3 is caused to flow into the control tank 6 as secondary waste water. In the control tank 6, the level of the secondary waste water flowing in is detected by the level meter 9, and the operation of the extraction pump 2 and the drainage pump 8 is controlled according to the amount of the water. Specifically, as described above, the water amount is detected in five stages, the entire wastewater treatment device M is stopped at the maximum upper limit a, the extraction pump 2 is stopped at the upper limit b, and the extraction pump 2 is extracted at the first lower limit c. The pump 2 is operated, the drainage pump 8 is operated at the second lower limit d, and the drainage pump 8 is stopped at the lowest limit e so that the amount of water in the control tank 6 is constantly maintained at an appropriate amount.

【0021】次に制御タンク6内の二次廃水を排水ポン
プ8で濾過フィルタ7A、7Bへ排水して該二次廃水中の
浮遊物質を濾過フィルタ7A、7B内に付着させて該二次
廃水を濾過した後、該濾過後の水を濾過水として下水あ
るいは河川等に放流する。なお濾過フィルタ7A、7Bは
必ずしも両方使用しなければならないものではなく、ど
ちらかをメンテナンス又は交換する際などには、所望の
前記開閉弁11A、11Bを閉じて片方だけ使用するように
してもよい。
Next, the secondary wastewater in the control tank 6 is drained to the filtration filters 7A and 7B by the drainage pump 8 and the suspended matter in the secondary wastewater is adhered to the filtration filters 7A and 7B so that the secondary wastewater is discharged. After being filtered, the filtered water is discharged as filtered water into sewage or a river. It is not always necessary to use both of the filtration filters 7A and 7B. When performing maintenance or replacement of either one, the desired on-off valves 11A and 11B may be closed and only one may be used. .

【0022】このようにして上記の作動を繰り返すと前
記濾過フィルタ7A、7B内への前記浮遊物質の付着が成
長して濾過フィルタ7A、7Bの内圧が高くなってくる。
本実施形態では濾過フィルタ7A、7Bに取り付けた前記
圧力センサ10A、10Bで、その内圧を常時検知してお
り、該内圧が所定値に達したら、濾過フィルタ7A、7B
内の図示されないフィルタユニットを付着、成長した前
記浮遊物質と共に取り出し、洗浄槽12にセットする。そ
して該洗浄槽12において前記フィルタユニットを図示さ
れないモ−タで回転させながら、図示されない配管から
洗浄水を供給することにより、浮遊物質を洗浄しながら
フィルタユニットから分離させる。その後、分離された
浮遊物質は洗浄水と共に前記真空濾過機13に送られて脱
水され固形化される。その後、この固形化された浮遊物
質は産業廃棄物として処分される。
When the above-described operation is repeated in this way, the adherence of the suspended matter in the filtration filters 7A and 7B grows, and the internal pressure of the filtration filters 7A and 7B increases.
In the present embodiment, the pressure sensors 10A and 10B attached to the filtration filters 7A and 7B constantly detect the internal pressure, and when the internal pressure reaches a predetermined value, the filtration filters 7A and 7B.
A filter unit (not shown) in the inside is taken out together with the adhered and grown floating substances, and set in the cleaning tank 12. Then, while the filter unit in the cleaning tank 12 is rotated by a motor (not shown), cleaning water is supplied from a pipe (not shown) to separate suspended substances from the filter unit while cleaning them. Then, the separated suspended solids are sent to the vacuum filter 13 together with washing water to be dehydrated and solidified. Then, the solidified suspended matter is disposed of as industrial waste.

【0023】なお本発明の実施の形態では、原水タンク
3に凝集剤滴下装置5を付設して原水タンク6内の一次廃
水中の浮遊物質を凝集させるようにしたが、これに限定
されるものではなく、制御タンク6内に凝集剤滴下装置5
を付設して制御タンク6内の二次廃水中の浮遊物質を凝
集させるようにしてもよい。
In the embodiment of the present invention, the raw water tank
Although the flocculant dropping device 5 is attached to 3 to flocculate suspended solids in the primary wastewater in the raw water tank 6, the flocculating agent dropping device 5 is not limited to this, and the flocculant dropping device 5 may be placed in the control tank 6.
May be additionally provided so that suspended substances in the secondary wastewater in the control tank 6 are aggregated.

【0024】また本発明の実施の形態では、脱水機とし
て真空濾過機13を用いたが、これに限定されるものでは
なく、脱水機としてフィルタ−プレス、ベルトフィルタ
−等を用いるようにしてもよい。
In the embodiment of the present invention, the vacuum filter 13 is used as the dehydrator, but the dehydrator is not limited to this, and a filter press, a belt filter or the like may be used as the dehydrator. Good.

【0025】[0025]

【発明の効果】本発明は上記の説明から明らかなよう
に、有水ガスホルダ内に溜められた水と油を一次廃水と
して抜出ポンプで原水タンクに送り込む工程と、該原水
タンク内の前記一次廃水に含まれる油を浮上させて浮上
油除去装置で除去した後、残りの水を二次廃水として制
御タンクへ流入させる工程と、該制御タンク内の前記二
次廃水を排水ポンプで濾過フィルタへ排水して該二次廃
水中の浮遊物質を濾過フィルタ内に付着させて該二次廃
水を濾過する工程と、該濾過後の水を濾過水として放流
する工程と、を有するから、処理済水は下水あるいは河
川にそのまま放流でき、浮遊物質のみを産業廃棄物とし
て処分すればよく、従来に比べて輸送費を含めた処理費
用を大幅に削減できると共に処理時間を大幅に短縮でき
る等種々に効果がある。
As is apparent from the above description, the present invention comprises a step of sending water and oil stored in a water-containing gas holder to a raw water tank as a primary waste water by a discharge pump, and the primary water in the raw water tank. After the oil contained in the wastewater is floated and removed by the floating oil removal device, the remaining water is allowed to flow into the control tank as secondary wastewater, and the secondary wastewater in the control tank is drained to a filtration filter. The treated water has the steps of draining and depositing the suspended solids in the secondary wastewater inside the filter to filter the secondary wastewater, and discharging the filtered water as filtered water. Can be discharged directly to sewage or rivers, and only suspended solids need to be disposed of as industrial waste, which can significantly reduce processing costs, including transportation costs, and significantly reduce processing time compared to conventional methods. But .

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施形態を示すフロ−チャ−ト図であ
る。
FIG. 1 is a flow chart showing an embodiment of the present invention.

【図2】制御タンクに設置したレベル計の詳細を示す図
である。
FIG. 2 is a diagram showing details of a level meter installed in a control tank.

【符号の説明】[Explanation of symbols]

1 有水ガスホルダ 1B 水 1C 油 2 抜出ポンプ 3 原水タンク 4 浮上油除去装置 5 凝集剤滴下装置 6 制御タンク 7A 7B 濾過フィルタ 8 排水ポンプ 9 レベル計 10A 10B 圧力センサ 13 脱水機 M 廃水処理装置 1 Water gas holder 1B water 1C oil 2 Extraction pump 3 Raw water tank 4 Floating oil remover 5 Flocculant dropping device 6 control tank 7A 7B Filtration filter 8 drainage pump 9 level meter 10A 10B Pressure sensor 13 dehydrator M wastewater treatment equipment

───────────────────────────────────────────────────── フロントページの続き (72)発明者 森本 秀樹 愛知県豊川市穂ノ原三丁目1番地 新東サ −ブラスト株式会社内 Fターム(参考) 4D015 BA19 BB05 CA06 DA04 DA23 EA35 FA01 FA14 4D051 AA01 BA09 4D066 BB01 BB31 EA03 EA06 EA11 FA01    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Hideki Morimoto             3-1, Honohara, Toyokawa City, Aichi Prefecture             -In Blast Co., Ltd. F-term (reference) 4D015 BA19 BB05 CA06 DA04 DA23                       EA35 FA01 FA14                 4D051 AA01 BA09                 4D066 BB01 BB31 EA03 EA06 EA11                       FA01

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 有水ガスホルダ内に溜められた水と油を
一次廃水として抜出ポンプで原水タンクに送り込む工程
と、該原水タンク内の前記一次廃水に含まれる油を浮上
させて浮上油除去装置で除去した後、残りの水を二次廃
水として制御タンクへ流入させる工程と、該制御タンク
内の前記二次廃水を排水ポンプで濾過フィルタへ排水し
て該二次廃水中の浮遊物質を濾過フィルタ内に付着させ
て該二次廃水を濾過する工程と、該濾過後の水を濾過水
として放流する工程と、を有することを特徴とする有水
ガスホルダ内の廃水処理方法。
1. A step of sending water and oil accumulated in a water-containing gas holder as a primary waste water to a raw water tank by an extraction pump, and floating the oil contained in the primary waste water in the raw water tank to remove floating oil. After removal by the device, a step of flowing the remaining water into the control tank as secondary wastewater, and draining the secondary wastewater in the control tank to a filtration filter with a drainage pump to remove suspended matter in the secondary wastewater. A method for treating wastewater in a water-containing gas holder, comprising: a step of adhering the secondary wastewater to a filtration filter to filter the secondary wastewater; and a step of discharging the filtered water as filtered water.
【請求項2】 前記制御タンクに流入される二次廃水の
水量に応じて前記抜出ポンプ及び排水ポンプの運転を制
御することを特徴とする請求項1記載の有水ガスホルダ
内の廃水処理方法。
2. The method for treating wastewater in a water-containing gas holder according to claim 1, wherein the operations of the extraction pump and the drainage pump are controlled according to the amount of secondary wastewater flowing into the control tank. .
【請求項3】 前記原水タンク内の一次廃水又は前記制
御タンク内の二次廃水に凝集剤を添加して該一次廃水中
又は該二次廃水中の浮遊物質を凝集させることを特徴と
する請求項1又は2のいずれかに記載の有水ガスホルダ
内の廃水処理方法。
3. A flocculating agent is added to the primary wastewater in the raw water tank or the secondary wastewater in the control tank to flocculate suspended solids in the primary wastewater or the secondary wastewater. Item 3. A method for treating wastewater in a water-containing gas holder according to item 1 or 2.
【請求項4】前記濾過フィルタ内に付着した浮遊物質を
該濾過フィルタから取り出して洗浄した後、脱水機によ
り脱水することを特徴とする請求項1乃至3のいずれかに
記載の有水ガスホルダ内の廃水処理方法。
4. The water-containing gas holder according to claim 1, wherein the suspended solids adhering to the inside of the filtration filter are taken out from the filtration filter, washed, and then dehydrated by a dehydrator. Wastewater treatment method.
【請求項5】 有水ガスホルダ内から抜出ポンプを介し
て抜き出された水と油を一次廃水として貯蔵する原水タ
ンクと、該原水タンクに付設されて、前記一次廃水から
浮上する油を除去する浮上油除去装置と、前記原水タン
クから流出される浮上油除去後の水を二次廃水として貯
蔵する制御タンクと、該制御タンクから排水ポンプを介
して排水された前記二次廃水中の浮遊物質が付着されて
該二次廃水を濾過する濾過フィルタと、を具備すること
を特徴とする有水ガスホルダ内の廃水処理装置。
5. A raw water tank for storing water and oil extracted from the water-containing gas holder via an extraction pump as primary waste water, and an oil attached to the raw water tank to remove floating oil from the primary waste water. A floating oil removing device, a control tank for storing the water after floating oil removal flowing out from the raw water tank as secondary wastewater, and a floating in the secondary wastewater drained from the control tank via a drainage pump. A waste water treatment device in a water-containing gas holder, comprising: a filtration filter to which a substance is attached to filter the secondary waste water.
【請求項6】 前記制御タンクに前記二次廃水の水量を
5段階に検知するレベル計を設置し、最上限では廃水処
理装置全体を停止させ、上限では前記抜出ポンプを停止
させ、第1下限では抜出ポンプを運転させ、第2下限では
前記排水ポンプを運転させ、最下限では排水ポンプを停
止させるようにしたことを特徴とする請求項5記載の有
水ガスホルダ内の廃水処理装置。
6. A level meter for detecting the amount of the secondary wastewater in five levels is installed in the control tank, the entire wastewater treatment device is stopped at the upper limit, and the extraction pump is stopped at the upper limit. 6. The wastewater treatment device in the water-containing gas holder according to claim 5, wherein the extraction pump is operated at the lower limit, the drainage pump is operated at the second lower limit, and the drainage pump is stopped at the lowest limit.
【請求項7】 前記原水タンク又は制御タンクに凝集剤
滴下装置を付設することを特徴とする請求項5又は6のい
ずれかに記載の有水ガスホルダ内の廃水処理装置。
7. The waste water treatment device in the water-containing gas holder according to claim 5, wherein a coagulant dropping device is attached to the raw water tank or the control tank.
【請求項8】 前記濾過フィルタに、その内圧を検知す
る圧力センサを取り付けたことを特徴とする請求項5乃
至7のいずれかに記載の有水ガスホルダ内の廃水処理装
置。
8. The wastewater treatment device in the water-containing gas holder according to claim 5, wherein a pressure sensor for detecting an internal pressure of the filtration filter is attached to the filtration filter.
【請求項9】 前記濾過フィルタから取り出されて洗浄
された浮遊物質を脱水する脱水機を具備することを特徴
とする請求項5乃至8のいずれかに記載の有水ガスホルダ
内の廃水処理装置。
9. The wastewater treatment device in the water-containing gas holder according to claim 5, further comprising a dehydrator for dehydrating the suspended matter taken out from the filtration filter and washed.
JP2002073421A 2002-03-18 2002-03-18 Treatment method for waste water in water-bearing gas holder and apparatus therefor Pending JP2003266061A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002073421A JP2003266061A (en) 2002-03-18 2002-03-18 Treatment method for waste water in water-bearing gas holder and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002073421A JP2003266061A (en) 2002-03-18 2002-03-18 Treatment method for waste water in water-bearing gas holder and apparatus therefor

Publications (1)

Publication Number Publication Date
JP2003266061A true JP2003266061A (en) 2003-09-24

Family

ID=29203089

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Application Number Title Priority Date Filing Date
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CN102701320A (en) * 2012-05-28 2012-10-03 中国石油天然气股份有限公司 Radial-flow closed circulating air-floating oil-removing tank and using method thereof
CN105439370A (en) * 2014-08-07 2016-03-30 中国石油化工股份有限公司 Technical method for processing refining and chemical wastewater by combination of biological aerated filter
CN105461108A (en) * 2015-11-30 2016-04-06 华电重工股份有限公司 Treatment method of semi-coke waste water
CN105984991A (en) * 2015-02-02 2016-10-05 江苏中金环保科技有限公司 Process for advanced treatment of sewage
CN108793531A (en) * 2018-06-18 2018-11-13 苏州科纵环保科技有限公司 A kind of multi-filtering processing mechanism of high oil-containing wastewater

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102701320A (en) * 2012-05-28 2012-10-03 中国石油天然气股份有限公司 Radial-flow closed circulating air-floating oil-removing tank and using method thereof
CN102701320B (en) * 2012-05-28 2013-11-06 中国石油天然气股份有限公司 Radial-flow closed circulating air-floating oil-removing tank and using method thereof
CN105439370A (en) * 2014-08-07 2016-03-30 中国石油化工股份有限公司 Technical method for processing refining and chemical wastewater by combination of biological aerated filter
CN105984991A (en) * 2015-02-02 2016-10-05 江苏中金环保科技有限公司 Process for advanced treatment of sewage
CN105984991B (en) * 2015-02-02 2019-01-01 江苏中金环保科技有限公司 A kind of sewerage advanced treatment process
CN105461108A (en) * 2015-11-30 2016-04-06 华电重工股份有限公司 Treatment method of semi-coke waste water
CN108793531A (en) * 2018-06-18 2018-11-13 苏州科纵环保科技有限公司 A kind of multi-filtering processing mechanism of high oil-containing wastewater
CN108793531B (en) * 2018-06-18 2021-10-29 永顺环保工业(太仓)有限公司 Multiple filtration treatment mechanism of high oily waste water

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