JP2002233863A - Method for treating waste water of hard roe seasoning liquid - Google Patents

Method for treating waste water of hard roe seasoning liquid

Info

Publication number
JP2002233863A
JP2002233863A JP2001077245A JP2001077245A JP2002233863A JP 2002233863 A JP2002233863 A JP 2002233863A JP 2001077245 A JP2001077245 A JP 2001077245A JP 2001077245 A JP2001077245 A JP 2001077245A JP 2002233863 A JP2002233863 A JP 2002233863A
Authority
JP
Japan
Prior art keywords
added
sodium
waste water
seasoning
seasoning liquid
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
JP2001077245A
Other languages
Japanese (ja)
Inventor
Toshikatsu Suzuki
敏勝 鈴木
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.)
PCS KK
Original Assignee
PCS KK
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 PCS KK filed Critical PCS KK
Priority to JP2001077245A priority Critical patent/JP2002233863A/en
Publication of JP2002233863A publication Critical patent/JP2002233863A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for treating waste water of a seasoning liquid to such a degree that it can be subjected to biological treatment as general waste water treatment. SOLUTION: 1) Waste water of a seasoning liquid is poured into a reaction vessel having pH adjusting function, sludge of biological treatment, aluminum sulfate and aluminum polychloride are added, an alkali agent such as sodium hydroxide, sodium carbonate or sodium bicarbonate is added to adjust the waste water to a very low acidity of pH 6.0±0.5 and sodium polyacrylate or a hydrolyzate of polyacrylamide as an anionic polymer flocculant is added to cause flocculation. 2) Hard flocks are formed by the above method and separated by floatation or precipitation as an ordinary separating operation, the treated water is biologically treated and the separated scum or precipitate is mixed with sludge of biological treatment and dehydrated.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明はサケ筋子などの魚卵
の調味液の使用後の排水の処理法に関するものである。 【0002】 【従来の技術】魚卵の調味液の使用後の排水はBODが
30万以上あり、通常の排水処理方法である生物処理に
は不向きで、塩分も強く、酸性で、油脂成分も含むた
め、簡単な凝集処理も、塩分と油脂分、蛋白質加水分解
物による影響で、強い凝集が起こらないため、簡単な一
次処理も出来ず、従来はバキュムカーで搬出して廃棄物
処理されていた。このため魚卵加工場にとって廃棄物処
理費が重い負担となっていた。 【0003】 【発明が解決しようとする課題】本発明は調味液の排水
を一般的な排水処理法である微生物処理法にかけられる
程度まで調味液の排水を処理する方法を提供する事であ
る。 【0004】 【課題を解決するための手段】本発明者は調味液の排水
の成分である、凝集を妨げていると考えられる塩分、油
脂、蛋白加水分解物等の成分に着目し鋭意研究した結
果、pH4から5の酸性を示す調味液の排水に硫酸バン
ド、ポリ塩化アルミニウム、塩化鉄等の無機凝集剤を添
加して、苛性ソーダ、炭酸ソーダ等のアルカリ剤でpH
を6±0.5に調整し、アニオン凝集剤で凝集させる方
法、あるいは調味液の排水に生物処理汚泥を添加してか
らカチオン性高分子凝集剤を添加し、その後硫酸バンド
あるいはポリ塩化アルミニウム等の無機凝集剤を添加し
て、苛性ソーダ、炭酸ソーダ等のアルカリ剤でpHを6
±0.5に調整し、アニオン性高分子凝集剤で凝集させ
る方法。これらの方法により従来凝集困難と見られてい
た調味液排水が強固な凝集フロックを形成して凝集し、
浮上分離、沈降分離などにより凝集フロックを分離して
処理水は生物処理に、浮上分離物(浮上スカム)あるい
は沈降物は生物処理汚泥と混合後脱水処理される。本発
明では従来酸性である調味液の凝集に重要なpH調整剤
として使用されるアルカリ剤としては苛性ソーダ等の強
アルカリ剤だけでなく、炭酸ソーダーなどの弱塩基も利
用できるという大きな特徴があり、このため処理作業も
容易になり危険性がなくなった。これは添加した後硫酸
バンドあるいはポリ塩化アルミニウム等の無機凝集剤の
金属イオンが調味液中の油脂分解物あるいは蛋白質加水
分解物に含まれる有機酸と結合して電離度を低下させた
為で、添加した無機凝集剤は酸性であるにもかかわら
ず、単独のアルカリ剤でpH調整するよりも、後硫酸バ
ンドあるいはポリ塩化アルミニウム等の無機凝集剤を添
加する事で、容易にpH調整出来る。このためアルカリ
剤の消耗も減少し、運転コストも低下する方法となっ
た。実際の処理装置では、調味液排水を、pH調整機能
を持った制御装置で制御された反応槽に流入させ、硫酸
バンド、ポリ塩化アルミニウムを添加後、苛性ソーダ、
炭酸ソーダー、重炭酸ソーダのアルカリ剤を添加してp
Hを6.0±0.5の微酸性に調整して、アニオン性高
分子凝集剤であるポリアクリル酸ソーダ、ポリアクリル
アマイド加水分解物を添加して凝集させて、脱水処理あ
るいは加圧浮上分離する。 【0005】 【発明の実施の形態】図面によって本発明の具体例を説
明する。図1は本発明の具体例のフローシートである。 【0006】 【発明の効果】本発明の方法では従来の廃棄物処理に比
べて、次のような利点がある。 (1)本発明の方法では従来は排水処理工程で処理が困
難とされていた調味液排水の発生現場で処理が可能とな
り、廃棄物処理のコストが大幅に低減される。 (2)本発明の方法では難解な部分が少なく、調整が極
めて容易な処理装置を構成できる為、応用範囲が広い。
このため加工工場排水の様な発生量が大きく異なる業態
にも、処理設備の大きさで対応できる。 (3)本発明の方法は、通常の工場排水処理工程及び微
生物処理の汚泥脱水工程に容易に付加出来るため、既成
の工場にも容易に処理工程を組み込める。 【0007】 【実施例1】筋子調味液BOD320000ppm20
0mlに濃度5000ppmの生物処理汚泥50ml加
え、カチオン性高分子凝集剤2ppm、ポリ塩化アルミ
ニウム150ppm添加後、苛性ソーダーでpH6.0
とした後、アニオン性高分子凝集剤6ppm凝集分離
し、沈殿物は強固なフロックを形成した。上澄みのBO
Dは130000ppmで1/3になった。 【実施例2】魚卵加工場排水BOD3000ppm40
0tに筋子調味液BOD320000ppm15t、濃
度5000ppmの生物処理汚泥5tを連続添加し、カ
チオン性高分子凝集剤5ppm、ポリ塩化アルミニウム
150ppm添加後、炭酸ソーダーでpH6.0とした
後、アニオン性高分子凝集剤12ppmを加えて凝集分
離し、浮上分離物は強固なフロックを形成した。加圧浮
上分離した結果処理水は4500ppmとなり、回分型
生物処理で処理された処理水は50ppmとなった。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating wastewater after use of a seasoning solution for fish eggs such as salmon sprouts. 2. Description of the Related Art Waste water after use of a seasoning solution for fish eggs has a BOD of 300,000 or more and is unsuitable for biological treatment which is a usual waste water treatment method, and has a strong salt content, is acidic, and has a fat and oil component. Because of this, simple coagulation treatment was not possible, and strong primary cohesion did not occur due to the effects of salts, oils and fats, and protein hydrolysates, so simple primary treatment was not possible.Conventionally, it was carried out in a vacuum car and disposed of as waste. . For this reason, waste disposal costs became a heavy burden on fish egg processing plants. An object of the present invention is to provide a method of treating seasoning liquid wastewater to such an extent that the seasoning liquid wastewater can be subjected to a microorganism treatment method which is a general wastewater treatment method. Means for Solving the Problems The present inventor has focused on the components of the drainage of the seasoning liquid, such as salts, fats and oils, and protein hydrolysates, which are considered to prevent coagulation. As a result, an inorganic coagulant such as a sulfuric acid band, polyaluminum chloride, and iron chloride was added to the drainage of the seasoning liquid having an acidity of pH 4 to 5, and the pH was adjusted with an alkaline agent such as sodium hydroxide and sodium carbonate.
Is adjusted to 6 ± 0.5 and flocculated with an anionic flocculant, or a biologically treated sludge is added to the drainage of the seasoning solution, and then a cationic polymer flocculant is added, and then a sulfate band or polyaluminum chloride, etc. And the pH is adjusted to 6 with an alkaline agent such as caustic soda and sodium carbonate.
A method of adjusting to ± 0.5 and coagulating with an anionic polymer coagulant. Seasoning liquid drainage, which was conventionally regarded as difficult to coagulate, forms a strong coagulated floc by these methods and coagulates,
The flocculated floc is separated by flotation separation, sedimentation separation, etc., and the treated water is subjected to biological treatment, and the floatation sediment (floating scum) or sediment is mixed with biological treatment sludge and then dewatered. In the present invention, as an alkaline agent used as a pH adjusting agent important for coagulation of a seasoning solution which is conventionally acidic, not only a strong alkaline agent such as caustic soda, but also a great feature that a weak base such as sodium carbonate can be used, For this reason, the processing work was facilitated and the danger was eliminated. This is because after addition, the metal ions of the inorganic flocculant such as the sulfate band or polyaluminum chloride are combined with the organic acid contained in the fat and oil decomposed product or the protein hydrolyzate in the seasoning liquid, thereby lowering the degree of ionization. Although the added inorganic flocculant is acidic, the pH can be easily adjusted by adding an inorganic flocculant such as a post-sulfuric acid band or polyaluminum chloride, rather than adjusting the pH with a single alkali agent. For this reason, the consumption of the alkali agent is reduced, and the operation cost is reduced. In an actual treatment device, the seasoning liquid wastewater is allowed to flow into a reaction tank controlled by a control device having a pH adjusting function, and after adding a sulfuric acid band and polyaluminum chloride, caustic soda,
Add sodium carbonate or sodium bicarbonate alkaline agent
H is adjusted to slightly acidic of 6.0 ± 0.5, and sodium polyacrylate and polyacrylamide hydrolyzate, which are anionic polymer coagulants, are added and coagulated, followed by dehydration treatment or pressure flotation. To separate. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing an embodiment of the present invention. FIG. 1 is a flow sheet according to an embodiment of the present invention. [0006] The method of the present invention has the following advantages over the conventional waste treatment. (1) According to the method of the present invention, it is possible to treat at the site where the seasoning liquid wastewater is generated, which has been conventionally difficult in the wastewater treatment step, and the cost of waste treatment is greatly reduced. (2) The method of the present invention has a small number of difficult parts and can be configured as an extremely easy-to-adjust processing apparatus, and thus has a wide range of applications.
For this reason, the size of the processing equipment can cope with business types in which the amount of generated wastewater, such as processing plant wastewater, varies greatly. (3) Since the method of the present invention can be easily added to the ordinary factory wastewater treatment step and the sludge dewatering step of microbial treatment, the treatment step can be easily incorporated into an existing factory. Example 1 Myosin seasoning liquid BOD320,000 ppm20
After adding 50 ml of biologically treated sludge having a concentration of 5000 ppm to 0 ml, adding 2 ppm of a cationic polymer flocculant and 150 ppm of polyaluminum chloride, the pH is adjusted to 6.0 with caustic soda.
After that, 6 ppm of an anionic polymer flocculant was flocculated and separated, and the precipitate formed a strong floc. The clear BO
D became 1/3 at 130,000 ppm. [Example 2] Drainage BOD 3000ppm40 of fish egg processing plant
0t, continuous addition of BIO320,000ppm15t, 5t of biologically treated sludge having a concentration of 5000ppm to 0t, addition of 5ppm of a cationic polymer flocculant and 150ppm of polyaluminum chloride, pH 6.0 with sodium carbonate, and anionic polymer flocculant 12 ppm was added to carry out coagulation separation, and the flotation product formed a strong floc. As a result of the pressure flotation separation, the treated water became 4500 ppm, and the treated water treated by the batch biological treatment became 50 ppm.

【図面の簡単な説明】 【図1】 本発明の方法のフローシート[Brief description of the drawings] FIG. 1 is a flow sheet of the method of the present invention.

Claims (1)

【特許請求の範囲】 【請求項1】魚卵の味付けに使用される漬け液の排水
(以下調味液排水と称する)を工場排水と混合し、硫酸
バンド、ポリ塩化アルミニウムを添加後、苛性ソーダ、
炭酸ソーダ重炭酸ソーダのアルカリ剤を添加してpHを
6.0±0.5に調整して、ポリアクリル酸ソーダ、ポ
リアクリルアマイド加水分解物等のアニオン性高分子凝
集剤を添加して凝集させて、加圧浮上分離する排水処理
方法。 【請求項2】 【請求項1】の調味液の排水を工場排水と混合する際に
生物処理曝気槽の汚泥を添加し混合した後に硫酸バン
ド、ポリ塩化アルミニウムを添加後、苛性ソーダ、炭酸
ソーダー、重炭酸ソーダのアルカリ剤を添加してpHを
6.0±0.5に調整して、ポリアクリル酸ソーダ、ポ
リアクリルアマイド加水分解物等のアニオン性高分子凝
集剤を添加して凝集させて、加圧浮上分離する排水処理
方法。 【請求項3】調味液の排水のみに生物処理曝気槽汚泥及
び硫酸バンド、ポリ塩化アルミニウムを添加後、苛性ソ
ーダ、炭酸ソーダー、重炭酸ソーダのアルカリ剤を添加
してpHを6.0±0.5に調整して、アニオン性高分
子凝集剤であるポリアクリル酸ソーダ、ポリアクリルア
マイド加水分解物を添加して凝集させて、脱水処理ある
いは加圧浮上分離する排水処理方法。 【請求項4】 【請求項1】、 【請求項2】、 【請求項3】で凝集し、加圧浮上分離した浮上スカムを
生物処理汚泥と混合し、脱水処理する事を特徴とする調
味液凝集物の脱水処理方法
Claims: 1. A drainage of a pickling solution used for seasoning a fish egg (hereinafter referred to as a seasoning solution drainage) is mixed with a factory drainage, and a sulfuric acid band and polyaluminum chloride are added.
The pH was adjusted to 6.0 ± 0.5 by adding an alkali agent of sodium carbonate and sodium bicarbonate, and an anionic polymer flocculant such as sodium polyacrylate and hydrolyzed polyacrylamide was added to cause aggregation. Wastewater treatment method of pressure flotation and separation. 2. The method of claim 1, wherein when the wastewater of the seasoning liquid is mixed with factory wastewater, sludge from a biological treatment aeration tank is added and mixed, and then a sulfuric acid band and polyaluminum chloride are added. The pH is adjusted to 6.0 ± 0.5 by adding an alkali agent of sodium bicarbonate, and an anionic polymer coagulant such as sodium polyacrylate or hydrolyzed polyacrylamide is added to cause coagulation. Wastewater treatment method with pressure flotation. 3. Addition of biological treatment aeration tank sludge, sulfate band, and polyaluminum chloride only to the drainage of seasoning liquid, and then addition of caustic soda, sodium carbonate, and sodium bicarbonate alkaline agents to adjust the pH to 6.0 ± 0.5. A wastewater treatment method in which sodium acrylate and polyacrylamide hydrolyzate, which are anionic polymer coagulants, are adjusted and coagulated, followed by dehydration treatment or flotation under pressure. 4. A seasoning characterized by mixing the floating scum which has been agglomerated and separated by pressure flotation with the biologically treated sludge and dewatering treatment. Dehydration method for liquid aggregates
JP2001077245A 2001-02-09 2001-02-09 Method for treating waste water of hard roe seasoning liquid Pending JP2002233863A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001077245A JP2002233863A (en) 2001-02-09 2001-02-09 Method for treating waste water of hard roe seasoning liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001077245A JP2002233863A (en) 2001-02-09 2001-02-09 Method for treating waste water of hard roe seasoning liquid

Publications (1)

Publication Number Publication Date
JP2002233863A true JP2002233863A (en) 2002-08-20

Family

ID=18934032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001077245A Pending JP2002233863A (en) 2001-02-09 2001-02-09 Method for treating waste water of hard roe seasoning liquid

Country Status (1)

Country Link
JP (1) JP2002233863A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100521649B1 (en) * 2003-09-24 2005-10-13 손을택 Small sewage terminal treatment method
JP2011088051A (en) * 2009-10-21 2011-05-06 Ihi Corp Waste liquid treatment equipment and waste liquid treatment method
CN105967302A (en) * 2016-05-05 2016-09-28 广州力必拓生物科技有限公司 Culture water environment total alkalinity conditioning agent and its use method and use

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100521649B1 (en) * 2003-09-24 2005-10-13 손을택 Small sewage terminal treatment method
JP2011088051A (en) * 2009-10-21 2011-05-06 Ihi Corp Waste liquid treatment equipment and waste liquid treatment method
CN105967302A (en) * 2016-05-05 2016-09-28 广州力必拓生物科技有限公司 Culture water environment total alkalinity conditioning agent and its use method and use
CN105967302B (en) * 2016-05-05 2019-07-30 广州力必拓生物科技有限公司 Cultivation water environment total alkalinity regulator and application method and application

Similar Documents

Publication Publication Date Title
JPH1057967A (en) Treatment of discharge water by coagulation settling method
JP4272122B2 (en) Coagulated water treatment method and apparatus
JP2002233863A (en) Method for treating waste water of hard roe seasoning liquid
US20210292195A1 (en) Anolyte as an additive for wastewater treatment
KR101088148B1 (en) Electrical neutralization of colloidal particles with speed control how water
KR20030053498A (en) The method and equipment of wastewater treatment contained organic compound of high concentration
JPH0144363B2 (en)
JP2002079004A (en) Aggregation method
JP2008149222A (en) Removal method of fluorine ions in hot spring water
JP2010162493A (en) Method and device for flocculation and sedimentation treatment of low organic compound concentration wastewater
KR101339305B1 (en) With electrical aggregation fluoride and treatment of wastewater containing hexavalent chromium
JP2000015007A (en) Flocculating method and flocculant
JPH07227599A (en) Treatment of waste tanning water containing chromium
JP7168301B2 (en) water treatment equipment
JPS59228993A (en) High-degree treatment of biological treating water
JPH1076275A (en) Wastewater treatment agent
JPS5832629B2 (en) Suspension flocculation treatment method
JP2002126755A (en) Coagulating separation method and coagulating separation treatment device
KR950002113B1 (en) Waste water treatment method
JP2004305893A (en) Solid-state waste water treating agent using artificial zeolite
KR20000024296A (en) emulsion type weist water treatment
JPS6048189A (en) Treatment of waste water
RU2158327C1 (en) Method of treatment of excessive circulating water of cardboard production for its reuse
RU2324659C1 (en) Method of purification of technological water
KR100206493B1 (en) Treatment of oil-containing waste water