JP2000024643A - Waste water discharging section - Google Patents

Waste water discharging section

Info

Publication number
JP2000024643A
JP2000024643A JP10197056A JP19705698A JP2000024643A JP 2000024643 A JP2000024643 A JP 2000024643A JP 10197056 A JP10197056 A JP 10197056A JP 19705698 A JP19705698 A JP 19705698A JP 2000024643 A JP2000024643 A JP 2000024643A
Authority
JP
Japan
Prior art keywords
storage tank
wastewater
water
ice
heat storage
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
JP10197056A
Other languages
Japanese (ja)
Inventor
Noriyoshi Nagase
徳美 永瀬
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP10197056A priority Critical patent/JP2000024643A/en
Publication of JP2000024643A publication Critical patent/JP2000024643A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Physical Water Treatments (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste water discharging section capable of efficiently purifying waste water by freezing and defrosting the waste water containing garbage or the like to effectively utilize energy and simultaneously to accelerate to destroy the structure of the garbage material. SOLUTION: An ice heat storage tank 3 into which the water containing the garbage or the like flows in, a heat combination supply device 6 for concentrating and separating the contained solid matter by the difference of the freezing rate by giving cold to the waste water in the ice heat storage tank and for defrosting the frozen water to enable to destroy the structure of the contained solid matter by the freezing operation and the defrosting operation and a waste water treating tank 4 for purifying the defrosted waste water are provided.

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、マンション等から
排出される厨芥排水、雑排水及び汚水の排水浄化処理で
発生する排水の浄化に係り、特に厨芥固形物を蓄熱媒体
として電源廃熱や工業廃熱及び夜間電力を利用して氷蓄
熱しそのエネルギーを利用する排水処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to purification of wastewater generated from condominiums and other wastewater produced in the treatment of wastewater from garbage, gray water and sewage, and more particularly to solid waste of kitchen refuse as a heat storage medium for power waste heat and industrial use. The present invention relates to a wastewater treatment device that stores ice heat using waste heat and nighttime electric power and uses the energy.

【0002】[0002]

【従来の技術】家電・コンピュータ・空調機器等の普及
により電力需要は年々急増し、特に夏期のピーク負荷は
増大傾向にある一方で、環境保全や発電所立地の困難等
の問題も多く電力設備を増強することも困難な状況にあ
る。このような中で、近年、余剰の安価な夜間電力等を
利用して夜の間に冷熱を貯蔵し昼間のピーク電力を平準
化する方法として、氷蓄熱を利用する方法が新築商業ビ
ルを中心に普及拡大してきている。
2. Description of the Related Art With the spread of home appliances, computers, air conditioners, etc., the demand for electric power has been increasing rapidly year by year, and the peak load especially in summer has been increasing. However, there are many problems such as environmental conservation and difficulty in locating a power plant. It is also difficult to increase the power. Under these circumstances, in recent years, as a method of storing excess heat during the night by using surplus inexpensive nighttime power and leveling the peak power in the daytime, the method using ice heat storage has been mainly used for newly built commercial buildings. It has been spreading.

【0003】従来の氷蓄熱方法は、 断熱密閉構造の氷
蓄熱槽内に充填された水道水等の冷媒又は蓄熱材に外部
熱源を介して冷熱が供給され、氷温下まで冷却されて凍
結処理されることとで冷熱エネルギーを氷の状態で貯蔵
し、必要時には断熱貯蔵された氷を融解して冷熱を回収
利用するというのがその基本である。
[0003] In the conventional ice heat storage method, cold heat is supplied to a refrigerant such as tap water or a heat storage material filled in an ice heat storage tank having an adiabatic closed structure via an external heat source, cooled to a temperature below ice temperature, and subjected to a freezing process. The basic principle is that the cold energy is stored in the form of ice, and the adiabatic stored ice is melted to recover and use the cold when necessary.

【0004】他方、水の使用量も年々増大しており限ら
れた水資源を汚れたまま垂れ流しにしないで、再利用す
るかもしくは環境に悪影響を与えないように浄化して放
水し、トータル的に水資源を保全していくことも重要な
取組みであるとの認識も高まっている。このような水資
源の保全に関しても、近年では、工場や企業単位、或い
は、地域単位で排水処理を行い浄化処理水を中水として
水洗トイレ用水や散水用水に再利用するようになり、新
築マンションや新興団地等の住居用地域でも同様の水再
利用の取組みが始まっている。
On the other hand, the amount of water used is increasing year by year, and limited water resources are not polluted and drained, but are reused or purified and discharged so as not to have an adverse effect on the environment. There is increasing recognition that conserving water resources is also an important initiative. In recent years, regarding the conservation of water resources, wastewater has been treated in factories, companies, or regions, and purified water has been reused as flush water for flush toilets and sprinkling water. Similar water reuse initiatives have also begun in residential areas such as and residential complexes.

【0005】また、レストランの厨房や家庭の台所で発
生する生ゴミ等の厨芥物の処理も、可燃ゴミの3割を占
め水分が多いために高温燃焼しにくく、家庭で廃棄処理
する上で最も嫌がられるものの1つである。
[0005] In addition, kitchen waste such as garbage generated in restaurant kitchens and home kitchens is difficult to burn at high temperature because it accounts for 30% of combustible garbage and has a large amount of water. It is one of the hated things.

【0006】厨芥物の処理においても前述の水処理に取
り込み、厨芥物を水処理浄化するシステムや汚水と共に
一括浄化するシステムが提案されてきており、厨房や台
所から直接的に処分されることもあって、ゴミ処分の手
間も省けるシステムとして注目されてきている。
[0006] In the treatment of kitchen garbage, a system for purifying kitchen garbage with water and a system for purifying the kitchen garbage together with sewage have been proposed. Therefore, it has been attracting attention as a system that can save the trouble of garbage disposal.

【0007】以上のように、氷蓄熱によるエネルギーの
平準化と厨芥物を含む排水処理は、環境保全及び住環境
改善に効果が大きく、また、両システムは共に液体を利
用または処理するという点で共通している。この共通点
に着目して、蓄熱機能と水処理機能をドッキングさせた
システムも既に提案され、たとえばビルディング等から
出る排水を直接利用して製氷し氷蓄熱する蓄熱方法が、
特開平6−18069号や特開平10−73290公報
に提案されている。
[0007] As described above, the leveling of energy by ice storage and the treatment of wastewater containing kitchen waste are highly effective for environmental preservation and improvement of the living environment, and both systems use or treat liquid. Have in common. Focusing on this common point, a system in which the heat storage function and the water treatment function are docked has already been proposed.For example, a heat storage method for making ice and storing ice by directly using wastewater from a building or the like has been proposed.
It has been proposed in JP-A-6-18069 and JP-A-10-73290.

【0008】特開平6−18069号公報に記載されて
いる氷蓄熱方法は、氷蓄熱槽内に導入された処理下水の
中に浸漬した伝熱管に冷媒供給装置から冷媒を供給循環
させて伝熱管周りに部分的に製氷し、後に残る不凍結残
水を槽外に排出する構成としたものであり、図5にその
概略を示す。
An ice heat storage method described in Japanese Patent Application Laid-Open No. 6-18069 discloses a method of supplying and circulating a refrigerant from a refrigerant supply device to a heat transfer tube immersed in treated sewage introduced into an ice heat storage tank. It is configured to partially make ice around and discharge remaining unfrozen residual water to the outside of the tank. FIG. 5 schematically shows the configuration.

【0009】図5において、被処理下水は下水受槽10
1に貯留され、下水送りポンプ102により取り出して
スクリーン装置103に送られ、粗ごみなどが除去され
る。スクリーン装置103で除去された粗ごみ類は排水
槽104に排出される。そして、粗ごみ類が除去された
被処理下水は油水分離装置105に送られて油分が分離
され、油分は排水槽104に排出され、粗ごみ類および
油分を除いた被処理下水は処理下水受槽106に貯留さ
れる。
In FIG. 5, the sewage to be treated is a sewage receiving tank 10.
1 and is taken out by the sewage feed pump 102 and sent to the screen device 103 to remove coarse dust and the like. The refuse removed by the screen device 103 is discharged to a drain tank 104. Then, the sewage to be treated from which the refuse is removed is sent to an oil-water separator 105 to separate the oil component, the oil component is discharged to a drainage tank 104, and the sewage to be treated excluding the refuse and the oil component is supplied to a treatment sewage receiving tank. Stored in 106.

【0010】氷蓄熱槽108内では、伝熱管に冷媒供給
装置から冷媒を供給循環させて伝熱管周りに製氷し、そ
の後に残る不凍結残水は残水排出ポンプ109により槽
外に排出される。氷蓄熱槽108内から不凍結残水を排
出する段階で、処理下水受槽106から一部の処理下水
を残水冷熱回収用熱交換器110に通して氷蓄熱槽10
8から排出される不凍結残水と冷熱交換を行い、不凍結
残水の保有する冷熱を処理下水に回収して冷処理下水と
して冷処理下水受槽111に貯留する。
In the ice heat storage tank 108, a refrigerant is supplied from the refrigerant supply device to the heat transfer tube and circulated to make ice around the heat transfer tube, and the remaining non-freezing residual water remaining thereafter is discharged out of the tank by the residual water discharge pump 109. . At the stage of discharging the unfrozen residual water from inside the ice heat storage tank 108, a part of the treated sewage is passed from the treated sewage receiving tank 106 through the heat exchanger 110 for recovering residual water cooling heat, and the ice heat storage tank 10
The non-freezing residual water discharged from 8 is subjected to cold heat exchange, and the cold stored in the non-freezing residual water is collected in the treated sewage and stored in the cold treated sewage receiving tank 111 as the cold treated sewage.

【0011】処理下水受槽106からの残りの処理下水
は中水冷熱回収用熱交換器118に通して冷処理下水受
槽111に貯留し、冷処理下水送りポンプ112によっ
て氷蓄熱槽108に送り込まれる。冷処理下水受槽11
1からの冷処理下水が氷蓄熱槽108から不凍結残水を
排水したあと、冷中水受槽116から冷中水循環ポンプ
121によって冷中水を氷蓄熱槽108に注入し、この
中水を負荷循環水として冷熱供給用熱交換器114およ
びポンプ113を含む負荷循環水ラインに循環させて、
伝熱管周りの氷の保有する冷熱を冷熱供給用熱交換器1
14を通して負荷115に供給する。
[0011] The remaining treated sewage from the treated sewage receiving tank 106 is stored in the chilled sewage receiving tank 111 through the middle water chilled heat recovery heat exchanger 118 and sent to the ice heat storage tank 108 by the chilled sewage feed pump 112. Cold treatment sewage receiving tank 11
After the cold treated sewage from 1 drains the unfrozen residual water from the ice heat storage tank 108, the cold water is injected into the ice heat storage tank 108 from the cold water receiving tank 116 by the cold water circulation pump 121, and the cold water is loaded. Circulating water as a circulating water through a load circulating water line including a cold heat supply heat exchanger 114 and a pump 113,
A heat exchanger 1 for supplying cold energy to the cold stored by the ice around the heat transfer tubes.
14 to a load 115.

【0012】冷熱供給用熱交換器114において冷熱の
回収が完了した氷蓄熱槽108中の氷解水を含む中水
は、冷中水として冷中水受槽116に排出し貯留され
る。冷中水受槽116から冷中水を冷中水送りポンプ1
17により取り出し、中水冷熱回収用熱交換器118に
通して処理下水と冷熱交換を行い、冷中水の保有する冷
熱を処理下水に回収する。この冷熱が回収された冷中水
は中水として中水槽119に貯留され、中水供給ポンプ
120により適宜に取り出されて便所用水などに使用さ
れる。
The cold water containing the thawed water in the ice heat storage tank 108 from which the cold heat has been completely recovered in the cold heat supply heat exchanger 114 is discharged as cold cold water into the cold cold water receiving tank 116 and stored. Cold and middle water feed pump 1 from the cold and middle water receiving tank 116
The cold water is taken out by 17 and passed through a heat exchanger 118 for recovering cold water from middle water to exchange heat with the treated sewage, and the cold stored in the cold water is recovered in the treated sewage. The cold water from which the cold energy has been recovered is stored in the middle water tank 119 as middle water, and is appropriately taken out by the middle water supply pump 120 and used as toilet water.

【0013】一方、特開平10−73290号公報に記
載のものは、氷製造部と蓄熱水槽を分離したもので、氷
蓄熱槽では製氷しないで、汚水はまず製氷機にかけられ
て製造した氷のみを分離し蓄熱水槽で氷の蓄積を行い、
氷以外の排水は製氷機から排出する構成としたものであ
る。図6にその概略を示す。
On the other hand, the apparatus disclosed in Japanese Patent Application Laid-Open No. Hei 10-73290 is one in which an ice producing unit and a heat storage water tank are separated from each other, and ice is not made in the ice heat storage tank. And accumulate ice in the heat storage water tank,
Wastewater other than ice is discharged from the ice machine. FIG. 6 shows the outline.

【0014】ビルディング等から出る各種排水は排水槽
201に貯蔵され、製氷機202に送られる。製氷機2
02は監視制御装置203によつて制御された夜間電力
により純粋な氷を製造するもので、この製氷機202で
製造された純氷は、氷蓄熱水槽204に蓄積される。製
氷機202は汚水を分離する機能が備えられたもので、
製氷機202で分離された汚水は、汚水処理装置205
に導入される。また、負荷側空調機206に使用した復
水も復水貯水槽207に導入され、復水も定期的に製氷
機202で純氷にされる。
Various wastewaters from buildings and the like are stored in a drainage tank 201 and sent to an ice maker 202. Ice machine 2
Numeral 02 is for producing pure ice by nighttime electric power controlled by the monitoring control device 203. Pure ice produced by the ice making machine 202 is accumulated in an ice heat storage water tank 204. The ice maker 202 is provided with a function of separating sewage,
The sewage separated by the ice making machine 202 is supplied to a sewage treatment apparatus 205.
Will be introduced. The condensate used for the load side air conditioner 206 is also introduced into the condensate water storage tank 207, and the condensate is also periodically made into pure ice by the ice maker 202.

【0015】[0015]

【発明が解決しようとする課題】しかしながら上記従来
の蓄熱方法および排水処理装置では、どちらも氷蓄熱に
おいて凍結させるのは排水中の一部の水分だけであり、
単に一部の水を再利用するのみで蓄熱槽における凍結解
凍処理によるメリットを十分に活かしていない。
However, in the above-mentioned conventional heat storage method and waste water treatment apparatus, only a part of the water in the waste water is frozen in the ice heat storage.
It merely reuses part of the water and does not fully exploit the benefits of freeze-thaw processing in the heat storage tank.

【0016】また、一般に、厨芥等の固形物はほとんど
が野菜屑や魚介類や肉類の残さや骨分であり、いずれも
生物細胞を含むものである。このため、厨房や台所のデ
ィスポーザー等の粉砕装置で厨芥自身は細かく砕かれて
はいるものの、特に繊維成分の野菜類はそれを構成して
いる細胞は破壊されにくい。したがって、後段の排水処
理槽において、生物処理等をするときには細胞膜や細胞
壁が一種の防護壁のような役割をするので処理時間が長
くなる原因ともなる。
In general, solids such as kitchen garbage are mostly vegetable waste, fish and shellfish and meat residues and bones, and all contain biological cells. For this reason, kitchen garbage itself is finely crushed by a crushing device such as a kitchen or kitchen disposer, but in particular, vegetables comprising fiber components are hardly destroyed by cells constituting the garbage. Therefore, when performing biological treatment or the like in the subsequent wastewater treatment tank, the cell membrane or cell wall functions as a kind of protective wall, which may cause a longer treatment time.

【0017】一方、野菜等は内部の含水量が非常に多い
ので、凍結解凍を行うと細胞壁や細胞膜が凍結の影響を
受けるものと解されるが、従来の技術では先に説明した
ように、凍結解凍処理は一部の水を再利用するためのも
のであって、後段の排水処理における処理能力の改善は
考慮されておらず、細胞膜の強い野菜等の厨芥の処理は
困難である。
On the other hand, vegetables and the like have a very high internal water content, and it is understood that cell walls and cell membranes are affected by freezing when subjected to freezing and thawing. The freeze-thaw treatment is for reusing a part of water, and no consideration is given to the improvement of the treatment capacity in the subsequent wastewater treatment, and it is difficult to treat garbage such as vegetables having a strong cell membrane.

【0018】そこで、本発明において解決すべき課題
は、蓄熱槽における厨芥等を含む排水の凍結解凍処理に
よって、エネルギーの有効利用を行ないつつ、厨芥物の
組織破壊を促進して効率的な排水浄化ができる排水処理
装置を提供することにある。
Therefore, the problem to be solved in the present invention is to promote efficient destruction of wastewater by promoting the destruction of the tissue of kitchen waste while effectively utilizing energy by freezing and thawing wastewater containing kitchen waste in the heat storage tank. It is an object of the present invention to provide a wastewater treatment device that can perform the treatment.

【0019】[0019]

【課題を解決するための手段】本発明は、厨芥等を含む
排水が流入する氷蓄熱槽と、前記氷蓄熱槽内の排水に冷
熱を与えて含有固形成分を凍結速度の違いにより濃縮分
離するとともにこの凍結した排水を解凍し、この凍結操
作と解凍操作により前記含有固形物の組織を破壊するこ
とができる熱併給装置と、解凍された排水を浄化処理す
る排水処理槽を備えたことを特徴とする。
SUMMARY OF THE INVENTION The present invention provides an ice heat storage tank into which wastewater containing kitchen waste and the like flows, and cools the wastewater in the ice heat storage tank to concentrate and separate solid components contained therein by a difference in freezing speed. A combined heat and heat supply device capable of defrosting the frozen wastewater and destroying the tissue of the solid content by the freezing and thawing operations, and a wastewater treatment tank for purifying the thawed wastewater. And

【0020】この構成では、厨芥排水の固形物の分離と
組織破壊によって浄化度が向上するとともに、水の再利
用と蓄熱によるエネルギーの有効利用が同時に行なえ
る。
With this configuration, the degree of purification is improved by separating solids from the kitchen wastewater and destructing the tissue, and water can be reused and energy can be effectively used by storing heat.

【0021】[0021]

【発明の実施の形態】請求項1に記載の発明は、厨芥等
を含む排水が流入する氷蓄熱槽と、前記氷蓄熱槽内の排
水に冷熱を与えて含有固形成分を凍結速度の違いにより
濃縮分離するとともにこの凍結した排水を解凍し、この
凍結操作と解凍操作により前記含有固形物の組織を破壊
することができる熱併給装置と、解凍された排水を浄化
処理する排水処理槽を備えたことを特徴とする排水処理
装置であるから、組織等が破壊された厨芥等を排水浄化
するので浄化速度が早くなる、あるいは、浄化度が向上
すると共に、水の再利用と蓄熱によるエネルギー有効利
用を同時に行なえるという作用を有する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention according to claim 1 is characterized in that an ice heat storage tank into which waste water including kitchen wastes flows in and a difference in the freezing rate of the solid component contained by applying cold to the waste water in the ice heat storage tank. The apparatus is provided with a cogeneration system capable of decomposing the frozen wastewater while concentrating and separating the frozen wastewater and destroying the tissue of the solid matter contained in the frozen and thawed operation, and a wastewater treatment tank for purifying the thawed wastewater. The wastewater treatment system is characterized by the fact that it cleans the garbage, etc., in which the tissue has been destroyed, so that the purification speed is increased, or the purification degree is improved, and the water is reused and the energy is efficiently used by storing heat. Can be performed simultaneously.

【0022】請求項2に記載の発明は、氷蓄熱槽には、
排水を上方位置から下方位置に向けて凍結させる凍結調
整部が設けられていることを特徴とする請求項1記載の
排水処理装置であるから、上方位置にはきれいな水を集
め下方位置には組織等が破壊されたペースト状固形物を
濃縮分離させることができ、上方位置のきれいな水を分
離抽出して再利用できるという作用を有する。
According to a second aspect of the present invention, in the ice heat storage tank,
The wastewater treatment apparatus according to claim 1, further comprising a freezing adjusting unit that freezes the wastewater from an upper position to a lower position, and collects clean water at an upper position and a tissue at a lower position. It is possible to concentrate and separate the paste-like solids that have been destroyed, etc., and have the effect that the clean water in the upper position can be separated and extracted and reused.

【0023】請求項3に記載の発明は、氷蓄熱槽には、
解凍された排水を濾過するための融解水濾過部が設けら
れている請求項1または2記載の排水処理装置であるか
ら、解凍排水から固形物と水を効率よく分離できるとい
う作用を有する。
According to a third aspect of the present invention, in the ice thermal storage tank,
The wastewater treatment device according to claim 1 or 2, further comprising a molten water filtration unit for filtering the thawed wastewater, which has an effect of efficiently separating solids and water from the thawed wastewater.

【0024】請求項4に記載の発明は、凍結調整部の下
側近傍位置に粗濾過部が設けられ、前記粗濾過部に残留
した固形成分を前記粗濾過された排水より先に前記熱併
給装置により凍結させることを特徴とする請求項1記載
の排水処理装置であるから、粗濾過で残留した厨芥等の
組織破壊が効率よく行われ、排水処理槽における浄化速
度がいっそう速くなる、あるいは、浄化度が更に向上す
るという作用を有する。
According to a fourth aspect of the present invention, a coarse filtration unit is provided at a position near the lower side of the freezing adjustment unit, and the solid component remaining in the coarse filtration unit is supplied to the co-heating unit before the coarsely filtered wastewater. Since the wastewater treatment device according to claim 1, wherein the wastewater treatment device is frozen by a device, tissue destruction of kitchen garbage and the like remaining by rough filtration is efficiently performed, and the purification speed in the wastewater treatment tank is further increased, or It has the effect of further improving the degree of purification.

【0025】請求項5に記載の発明は、氷蓄熱槽で分離
された固形物を含んだ排水を加熱する排水温度調整手段
を備えたことを特徴とする請求項1から4のいずれかに
記載の排水処理装置であるから、排水処理槽に流入する
排水温度を排水処理に適した温度に調整でき、排水処理
槽の性能を安定化させるという作用を有する。
According to a fifth aspect of the present invention, there is provided the drainage temperature adjusting means for heating the wastewater containing the solid matter separated in the ice heat storage tank. Therefore, the temperature of the wastewater flowing into the wastewater treatment tank can be adjusted to a temperature suitable for wastewater treatment, and has the effect of stabilizing the performance of the wastewater treatment tank.

【0026】なお、本発明において、濃縮分離とは、厨
芥排水を凍結するときに水と含有固形成分の凍結速度の
違いから清浄な水の方から凍結し、このために含有固形
成分は徐々に濃縮されて変性凝集し、その後に解凍する
と水分は容易に脱水されて最後に固形分がペースト状に
なって残留することをいう。
In the present invention, the concentration separation means that when kitchen wastewater is frozen, free water is frozen from the clean water due to the difference in the freezing speed of water and the solid component contained therein. When concentrated and denatured and coagulated, and then thawed, the water is easily dehydrated, and finally the solid remains in the form of a paste.

【0027】以下、図面に示す実施の形態による本発明
を具体的に説明する。図1は本発明の一実施の形態によ
る排水処理装置の全体構成図を示す。
Hereinafter, the present invention according to the embodiment shown in the drawings will be specifically described. FIG. 1 shows an overall configuration diagram of a wastewater treatment apparatus according to an embodiment of the present invention.

【0028】図1において、排水処理装置1は、厨芥物
を含む排水や雑排水を一次的に貯留し後段の処理量を調
整するための一次貯留槽2、この一次貯留槽2と配管結
合されて厨芥物を含む排水や雑排水を凍結処理及び解凍
処理を行なう傍ら蓄熱槽としての効果を発揮する氷蓄熱
槽3、この氷蓄熱槽3から排出される排水を浄化処理す
る排水処理槽4、主に氷蓄熱槽3を冷却・加熱する熱エ
ネルギーを発生及び利用する熱併給装置6を備えたもの
である。電源部40によって運転動作される熱併給装置
6には、この熱併給装置6からの冷温熱の供給を受けて
ビル内や室内の空調を行う空調ユニット8が接続されて
いる。また、一次貯留槽2は、トイレ,洗面所,洗濯
機,お風呂から排出される雑排水を供給する下水配管1
0に接続したもので、この下水配管10にはビルの厨房
や家庭の台所に設置されて生ゴミを粉砕処理するための
ディスポーザ9からの流路が連結されている。
In FIG. 1, a wastewater treatment apparatus 1 is a primary storage tank 2 for temporarily storing wastewater including kitchen waste and miscellaneous wastewater and adjusting the amount of wastewater to be treated in a later stage, and is connected to the primary storage tank 2 by piping. An ice heat storage tank 3 that performs an effect as a heat storage tank while performing freezing and thawing treatment of waste water and miscellaneous waste water containing kitchen waste, a waste water treatment tank 4 that purifies waste water discharged from the ice heat storage tank 3, The apparatus is provided with a cogeneration system 6 for generating and utilizing heat energy for cooling and heating the ice heat storage tank 3. An air-conditioning unit 8 is connected to the heat and heat supply device 6 that is operated and operated by the power supply unit 40 and receives air from the heat and heat supply device 6 to cool and heat the inside of a building or a room. The primary storage tank 2 is a sewage pipe 1 for supplying miscellaneous wastewater discharged from a toilet, a washroom, a washing machine, and a bath.
The sewage pipe 10 is connected to a flow path from a disposer 9 installed in a building kitchen or a home kitchen for crushing garbage.

【0029】なお、熱併給装置6としては、冷熱と温熱
を発生及び利用できるいかなる熱サイクル装置であって
もよいが、発電所や工業地帯における廃熱を利用すれば
電源40の使用量を削減でき省エネルギーとなり得るの
で、そのような場合は廃熱を利用できるヒートポンプ又
は吸収式冷凍サイクルのような手段が望ましい。
The heat cogeneration device 6 may be any heat cycle device that can generate and use cold and hot heat, but the use of the power source 40 can be reduced by using waste heat in a power plant or an industrial area. In such a case, a means such as a heat pump or an absorption refrigeration cycle that can use waste heat is desirable because energy can be saved.

【0030】また、以上のような各機器の配列におい
て、排水処理装置1には、一次貯留槽2に貯留された排
水を氷蓄熱槽3に移送制御するための排水供給ポンプ1
1、氷蓄熱槽3からの解凍水を排水処理槽4に移送制御
する解凍水排出ポンプ12、氷蓄熱槽3の解凍処理時の
初期融解水を放水するための初期融解水ポンプ13がそ
れぞれ組み込まれる。
In the arrangement of the above-described devices, the wastewater treatment apparatus 1 includes a wastewater supply pump 1 for controlling the transfer of wastewater stored in the primary storage tank 2 to the ice heat storage tank 3.
1. A thawing water discharge pump 12 for controlling the transfer of the thawing water from the ice heat storage tank 3 to the wastewater treatment tank 4, and an initial melting water pump 13 for discharging the initial melting water during the thawing processing of the ice heat storage tank 3 are incorporated. It is.

【0031】氷蓄熱槽3の内部には、凍結融解処理時に
初期融解水を取り出し固形物を濾過残留させるための濾
過部21を設けるとともに、上部側及び下部側には熱併
給装置6に接続され厨芥排水を凍結融解して熱エネルギ
ーを蓄熱する上方氷蓄熱槽熱交換器30aと下方氷蓄熱
槽熱交換器30bをそれぞれ配置する。
Inside the ice heat storage tank 3, there is provided a filtration unit 21 for taking out the initial melt water during the freeze-thaw treatment and filtering and remaining solid matter, and is connected to the co-heating unit 6 on the upper and lower sides. An upper ice storage tank heat exchanger 30a and a lower ice storage tank heat exchanger 30b that freeze-thaw the kitchen wastewater and store heat energy are disposed, respectively.

【0032】また、排水処理槽4の内部には、生物処理
または凝集処理または電解浄化等により排水の浄化を行
う浄化処理部22とこの浄化処理部22からの処理水の
汚泥を沈降させる沈降部23とを設ける。浄化処理部2
2には、その内部の温度調整のために熱併給装置6に接
続した加熱用熱交換器32を組み込んでいる。また、沈
降部23は、その内部で汚泥24とこの汚泥24が沈降
して浄化された処理水25に分離可能としたものであ
り、処理水25を中水利用施設等に配水するためにポン
プ15を介して放水配管26を接続している。
In the wastewater treatment tank 4, a purification treatment section 22 for purifying wastewater by biological treatment, coagulation treatment, electrolytic purification, or the like, and a sedimentation section for sedimenting the sludge of the treated water from the purification treatment section 22 are provided. 23 are provided. Purification processing unit 2
2 incorporates a heating heat exchanger 32 connected to the cogeneration system 6 for temperature adjustment inside. The settling unit 23 is capable of separating sludge 24 therein and treated water 25 in which the sludge 24 has settled and purified, and a pump for distributing the treated water 25 to a wastewater utilization facility or the like. A water discharge pipe 26 is connected through the connection 15.

【0033】以上の構成において、排出される厨芥生ゴ
ミは、ビルの厨房や家庭の台所に設置されたディスポー
ザ9で水の供給を受けながら粉砕処理され、厨房粉砕物
として一次貯留槽2へ排出される。同時に洗面所や洗濯
機からの雑排水も下水配管10を介して一次貯留槽2へ
排出される。そして、一次貯留槽2で一次貯留された排
水は、排水供給ポンプ11の運転制御により氷蓄熱槽3
へ供給される。
In the above arrangement, the kitchen garbage discharged is pulverized while being supplied with water by a disposer 9 installed in a kitchen of a building or a home kitchen, and discharged to the primary storage tank 2 as a crushed product of the kitchen. Is done. At the same time, miscellaneous wastewater from the washroom and the washing machine is also discharged to the primary storage tank 2 through the sewage pipe 10. Then, the wastewater primarily stored in the primary storage tank 2 is supplied to the ice heat storage tank 3 by the operation control of the drainage supply pump 11.
Supplied to

【0034】氷蓄熱槽3では、熱併給装置6と接続され
た上方氷蓄熱槽熱交換器30a及び下方氷蓄熱槽熱交換
器30bにより、氷蓄熱槽3に流入する一次貯留槽2か
らの排水を氷温以下にして一度凍結させた後、氷温以上
の温度にして融解処理を行なう。
In the ice heat storage tank 3, drainage from the primary storage tank 2 flowing into the ice heat storage tank 3 is performed by the upper ice heat storage tank heat exchanger 30 a and the lower ice heat storage tank heat exchanger 30 b connected to the cogeneration unit 6. Is frozen at a temperature below the ice temperature, and then thawed at a temperature above the ice temperature.

【0035】ここで、氷蓄熱槽3では、排水の凍結融解
処理はバッチ式で処理が行われる。すなわち、日中間に
発生した処理水は一次貯留槽2に貯えられ、夜間の早い
時期に排水供給ポンプ11を運転制御して氷蓄熱槽3に
移送される。氷蓄熱槽3に一定量の排水が貯まった状態
になったら熱併給装置6を運転して上方氷蓄熱槽熱交換
器30a及び下方氷蓄熱槽熱交換器30bに冷熱を送り
込み、凍結処理を開始して、氷蓄熱槽3の内容物を凍結
させる。
Here, in the ice heat storage tank 3, the freezing and thawing treatment of the waste water is performed in a batch system. That is, the treated water generated during the middle of the day is stored in the primary storage tank 2 and is transferred to the ice heat storage tank 3 by controlling the operation of the drainage supply pump 11 at an early time at night. When a certain amount of wastewater is stored in the ice heat storage tank 3, the cogeneration unit 6 is operated to send cold heat to the upper ice heat storage tank heat exchanger 30a and the lower ice heat storage tank heat exchanger 30b to start the freezing process. Then, the contents of the ice heat storage tank 3 are frozen.

【0036】上方氷蓄熱槽熱交換器30aは氷蓄熱槽3
の上方に位置しているので、まず上方氷蓄熱槽熱交換器
30aに冷熱を送り込むと凍結過程は上方から始まり、
徐々に下方へ広がる。すなわち、上側から下側へ段々と
凍結していく。なお、氷蓄熱槽熱交換器は2個に限らず
幾つ配置してもよく、上側から下側へ段々と凍結してい
くようにできればよい。
The upper ice storage tank heat exchanger 30a is an ice storage tank 3
Is located above, first, when the cold heat is sent to the upper ice storage tank heat exchanger 30a, the freezing process starts from above,
It gradually spreads downward. That is, it freezes gradually from the upper side to the lower side. Note that the number of the ice storage tank heat exchangers is not limited to two, and any number may be provided, as long as the heat can be gradually frozen from the upper side to the lower side.

【0037】以下に、凍結の状況について説明する。水
溶液の凍結においては、純粋な水の凍結開始温度は0℃
である。しかし、厨芥等を含む水溶液の場合は、水の凝
固点降下が生じて厨芥等固形成分の濃度に相関して凍結
する温度は低下していく。
Hereinafter, the frozen state will be described. In the freezing of an aqueous solution, the freezing start temperature of pure water is 0 ° C.
It is. However, in the case of an aqueous solution containing kitchen waste or the like, the freezing point of water is lowered, and the freezing temperature is reduced in correlation with the concentration of solid components such as kitchen waste.

【0038】いま、氷蓄熱槽3の上方氷蓄熱槽熱交換器
30aを氷点温度以下にすると、上方氷蓄熱槽熱交換器
30aの近傍の水溶液は凍結しようとする。このとき、
撹拌等を加えずに静かに凍結を行なうと、厨芥等固形成
分の濃度の低いすなわち凍結する温度が高い水溶液のと
ころから凍結を開始していく。結果として、凍結してい
く過程において、より固形成分の少ない真水に近い氷の
層が上方氷蓄熱槽熱交換器30aの近傍に形成され、上
方氷蓄熱槽熱交換器30aから遠ざかるほど固形成分の
多い氷の層が形成される。
Now, when the temperature of the upper heat storage tank heat exchanger 30a of the ice heat storage tank 3 is lowered below the freezing point, the aqueous solution near the upper heat storage tank heat exchanger 30a tends to freeze. At this time,
When freezing is performed gently without adding agitation or the like, freezing starts from an aqueous solution having a low concentration of solid components such as kitchen waste, that is, a high freezing temperature. As a result, in the process of freezing, a layer of ice closer to fresh water having less solid components is formed near the upper ice storage tank heat exchanger 30a, and the solid components become more distant from the upper ice storage tank heat exchanger 30a. Many ice layers are formed.

【0039】上方氷蓄熱槽熱交換器30aは氷蓄熱槽3
の上部側に位置しているので、重力による固形成分の沈
降効果も加わりながら凍結過程は上方から始まり、徐々
に下方へ広がるので、上方にきれいな氷が形成され、上
側から下側へ段々と固形成分の多い氷が形成される。一
定時間後に、氷蓄熱槽3の上方氷蓄熱槽熱交換30a付
近から下方氷蓄熱槽熱交換器30bが配置された部分の
近傍まで凍結が進んできたら、下方氷蓄熱槽熱交換器3
0bに冷熱を供給して氷蓄熱槽3の下方も凍結させる。
The upper ice storage tank heat exchanger 30a is an ice storage tank 3
The freezing process starts from the top and gradually spreads downward, adding the sedimentation effect of the solid component due to gravity, so that clean ice is formed upward, and solids gradually increase from the top to the bottom. Rich ice is formed. After a certain period of time, if the freezing has progressed from the vicinity of the upper ice storage tank heat exchanger 30a of the ice storage tank 3 to the vicinity of the portion where the lower ice storage tank heat exchanger 30b is disposed, the lower ice storage tank heat exchanger 3
0b is supplied with cold heat to freeze below the ice heat storage tank 3 as well.

【0040】氷蓄熱槽3の全体が凍結すると、最終的に
は沈降していた厨芥物等の固形物も凍結してしまう。こ
のとき、厨芥物に含まれる野菜屑等は、それらを構成す
る細胞内の溶液及び組織も凍結するので、凍結時の氷の
体積膨張と凍結変性の効果によって野菜屑等の細胞は破
壊されて脆くなる。
When the whole of the ice heat storage tank 3 is frozen, finally solidified substances such as kitchen refuse which have settled are also frozen. At this time, vegetable scraps and the like contained in kitchen waste also freeze the solution and tissue in the cells constituting them, so that the cells such as vegetable scraps are destroyed by the effects of ice volume expansion and freeze denaturation during freezing. Becomes brittle.

【0041】そして、翌日、氷蓄熱槽3の上方氷蓄熱槽
熱交換器30a及び下方氷蓄熱槽熱交換器30bによっ
て冷熱を回収しつつ、凍結された排水は解凍処理され
る。この回収冷熱をビル内や室内に設置された空調ユニ
ット8に回して冷房等の熱源として利用する。
On the next day, the frozen wastewater is thawed while recovering the cold heat by the upper heat storage tank heat exchanger 30a and the lower heat storage tank heat exchanger 30b of the ice heat storage tank 3. The recovered cold heat is sent to an air conditioning unit 8 installed in a building or a room to be used as a heat source for cooling or the like.

【0042】以上のような凍結融解処理を行うと、厨芥
物等の固形物も凍結されその後解凍されるので、特に含
水量の多い野菜類の生ゴミは氷の膨張変形及び凍結融解
による変性によって組織細胞は破壊される。また、凝固
点降下の影響により上方に清浄な水の氷ができてその後
に解凍されるので、上方氷蓄熱槽熱交換器30aの方か
ら排水を解凍させると、解凍時の初期融解水は固形成分
の少ない水として溶け出してくる。これを濾過部21を
介して初期融解水ポンプ13を運転制御して放水管26
へ放水する。これにより、氷蓄熱槽3内の排水は放出し
た清浄な水の分だけ濃縮されることになる。また、解凍
処理後、排水は排水処理槽4へ搬送される。
When the above-mentioned freeze-thaw treatment is performed, solids such as kitchen garbage are also frozen and then thawed, so that vegetable garbage having a high water content is particularly degraded by the expansion deformation of ice and the denaturation by freeze-thawing. Tissue cells are destroyed. In addition, ice of clean water is formed upward due to the influence of freezing point depression and then thawed. Therefore, when the wastewater is thawed from the upper heat storage tank heat exchanger 30a, the initial melting water at the time of thawing becomes solid component. Melts out as water with little water. This is controlled by the operation of the initial molten water pump 13 through the filtration unit 21 to discharge the water from the discharge pipe 26.
Water. As a result, the wastewater in the ice heat storage tank 3 is concentrated by the amount of the released clean water. After the thawing process, the wastewater is transported to the wastewater treatment tank 4.

【0043】このように、本発明では排水中の厨芥につ
いての凍結解凍処理における厨芥の変性凝集が可能であ
り、固液分離を容易化することができる。ここで、排水
中の厨芥の変性凝集について説明する。
As described above, according to the present invention, the garbage in the wastewater can be denatured and coagulated in the freezing and thawing treatment, and the solid-liquid separation can be facilitated. Here, the denaturation and aggregation of kitchen waste in drainage will be described.

【0044】粉砕された厨芥等固形物が懸濁状態になっ
ている状態では、粉砕された厨芥等固形物の粒子の周囲
に結合力の弱い間隙水が存在する。このような間隙水を
含む粉砕された厨芥等固形物を含む厨芥排水を凍結させ
ると、まず、純度が高く凝固点が高い水の所から凍結を
開始し、氷が成長していくようにして凍結する。これに
よって、固形物間に存在する間隙水は成長していく氷に
容易に吸い出されて無くなり、結果として粉砕された厨
芥物等固形物どうしは近づいて凝集する。さらに凍結温
度を下げて凍結が進むと、粉砕された厨芥物等固形物の
構成としての生ゴミ等の細胞内部の内部水が凍結して細
胞壁が破壊されて内部水も吸い出される。これによって
さらに凝集性が向上するとともに脱水性も向上する。
In a state in which the solids such as the crushed garbage are in a suspended state, pore water having a weak binding force exists around the particles of the solids such as the crushed garbage. When freezing garbage wastewater containing solid matter such as crushed garbage containing pore water, it starts freezing from water with high purity and a high freezing point, and freezes as the ice grows. I do. As a result, the pore water existing between the solids is easily sucked out by the growing ice and disappears, and as a result, the solids such as the crushed garbage approach and aggregate. When the freezing temperature is further reduced and the freezing proceeds, the internal water inside the cells such as garbage as a solid material such as crushed garbage is frozen, the cell wall is broken, and the internal water is also sucked out. This further improves cohesion and dehydration.

【0045】以上により、凍結解凍処理した結果、懸濁
状態にあった厨芥等固形物は凝集して脱水しやすくな
り、したがって固液分離が容易に行なえるようになる。
従来ではこのような変性凝集による固液分離についての
技術思想はなく、凍結操作と変性凝集によって濃縮分離
が容易にかつ効果的に得られる。
As described above, as a result of the freeze-thaw treatment, solids such as kitchen garbage in a suspended state are easily aggregated and dehydrated, so that solid-liquid separation can be easily performed.
Conventionally, there is no technical idea about such solid-liquid separation by denaturation aggregation, and concentration and separation can be easily and effectively obtained by freezing operation and denaturation aggregation.

【0046】一方、排水処理槽4の浄化処理部22で
は、主に排水中の固形物の分解または凝集の処理と溶解
性有機成分の固定化や分解・酸化処理を行い、排水を浄
化し、浄化処理部22で発生した汚泥24は沈降部23
で下方へ沈降するので、浄化処理水25は放水するに望
ましい浄化された水となる。処理水25は放水管26よ
り中水利用施設等へ放水され、沈降した汚泥24は定期
的にバキュームカー等で吸引して外部へ取り出す。
On the other hand, the purification treatment section 22 of the wastewater treatment tank 4 mainly purifies wastewater by decomposing or coagulating solids in the wastewater and fixing, decomposing and oxidizing soluble organic components. The sludge 24 generated in the purification processing section 22
, And the purified water 25 becomes purified water which is desirable to discharge. The treated water 25 is discharged from a water discharge pipe 26 to an intermediate water utilization facility or the like, and the settled sludge 24 is periodically sucked out by a vacuum car or the like and taken out.

【0047】また、浄化処理部22における浄化処理の
手段が生物処理方法等の水温の影響を受け易い場合に
は、極端な温度低下は処理能力維持上好ましくないの
で、特に低温になる場合には加熱用熱交換器32により
加熱保温することが好ましい。
Further, when the purification means in the purification section 22 is susceptible to the temperature of water such as a biological treatment method, an extreme decrease in temperature is not preferable for maintaining the treatment capacity. It is preferable to heat and keep the temperature by the heating heat exchanger 32.

【0048】図2は本発明の別の実施の形態による排水
処理装置の全体構成図を示す。この例は、図1の構成に
おける下方氷蓄熱槽熱交換器30bに代えて、粗濾過パ
ネル19を回転可能に備えた点が異なり、その他の構成
は同じである。なお、図1の例と同じ構成部材について
は共通の符号で指示し、その詳細な説明は省略する。
FIG. 2 shows an overall configuration diagram of a wastewater treatment apparatus according to another embodiment of the present invention. This example is different in that a coarse filtration panel 19 is rotatably provided instead of the lower ice heat storage tank heat exchanger 30b in the configuration of FIG. 1, and the other configuration is the same. Note that the same components as those in the example of FIG. 1 are designated by the same reference numerals, and detailed description thereof will be omitted.

【0049】粗濾過パネル19は板状材に多数の孔を開
けたもので、氷蓄熱槽3の内部に組み込まれ一次貯留槽
2からの生ゴミ等を含む排水中の比較的大きな固形物を
濾過する。そして、モータを利用した粗濾過パネル駆動
部20によって回転制御され凍結・解凍処理した固形物
を排水中に落とす役割を持つ。
The coarse filter panel 19 is a plate-like material having a large number of holes formed therein. The coarse filter panel 19 is incorporated in the ice heat storage tank 3 and removes relatively large solid matter in wastewater including garbage from the primary storage tank 2. Filter. Then, it has a role of dropping the solid matter subjected to the freeze / thaw processing under the rotation control by the coarse filtration panel drive unit 20 using a motor into the wastewater.

【0050】図3は粗濾過パネル19とその駆動部を示
す概略図であり、上方氷蓄熱槽熱交換器30aに干渉し
ないようにするため、図中の矢印で示す範囲で回動する
ように制御する。
FIG. 3 is a schematic view showing the coarse filtration panel 19 and its driving section. In order not to interfere with the upper ice storage tank heat exchanger 30a, the panel is rotated in the range indicated by the arrow in the figure. Control.

【0051】粗濾過パネル10の孔を通り抜ける固形分
の通過粒径は、ディスポーザ9で粉砕された野菜屑等の
固形物が残留する0.5〜5.0mm程度であり、1m
m程度のとすることが好ましい。なお、粗濾過パネル1
9は、左右を歯車結合した観音開き構造やロール式に巻
き込む方式等、比較的大きな固形物の残留とその後の排
出ができるものであればいずれでもよい。
The passing particle size of the solids passing through the holes of the coarse filtration panel 10 is about 0.5 to 5.0 mm in which solids such as vegetable chips pulverized by the disposer 9 remain, and is 1 m.
m is preferable. In addition, the coarse filtration panel 1
Reference numeral 9 may be any type, such as a double-opening structure in which the left and right are gear-coupled or a roll-in type, as long as a relatively large solid can be retained and subsequently discharged.

【0052】図2に示す排水浄化装置において、一次貯
留槽2から排水が氷蓄熱槽3へ供給されるときに、粗濾
過パネル19は図3に示すようにほぼ水平の姿勢に保持
されている。そして、供給された生ゴミ等を含む排水は
粗濾過パネル19に当たって粗濾過され、粗濾過パネル
19の上には比較的大きな固形物としての厨芥物が残留
する。このとき、比較的大きな固形物としての厨芥物が
粗濾過パネル19の上に残っていることとその近傍に上
方氷蓄熱槽熱交換器30aが配置されていることから、
上方氷蓄熱槽熱交換器30aに冷熱を供給すると粗濾過
パネル19上の残留厨芥物が先行して凍結していく。
In the waste water purifying apparatus shown in FIG. 2, when waste water is supplied from the primary storage tank 2 to the ice heat storage tank 3, the coarse filtration panel 19 is held in a substantially horizontal posture as shown in FIG. . Then, the supplied wastewater containing garbage and the like hits the coarse filtration panel 19 and is roughly filtered, and relatively large solid garbage remains on the coarse filtration panel 19. At this time, since the relatively large solid garbage remains on the rough filtration panel 19 and the upper ice heat storage tank heat exchanger 30a is disposed in the vicinity thereof,
When cold heat is supplied to the upper ice storage tank heat exchanger 30a, residual kitchen waste on the coarse filtration panel 19 freezes first.

【0053】粗濾過パネル19を設けた構成では、その
上に残留する厨芥物が上方氷蓄熱槽熱交換器30aの近
傍に置かれることになるので、野菜屑の組織細胞の破壊
は氷蓄熱槽3の全体を凍結させなくても達成できる。し
たがって、例えば、蓄熱量が少ない場合でも氷蓄熱槽3
全体を凍結させる必要がなく、十分な冷熱の蓄熱ができ
ないときでも野菜屑の組織細胞の破壊を行なうことがで
き、後段の排水処理槽4の処理性能を安定化させること
ができる。
In the configuration in which the coarse filtration panel 19 is provided, the kitchen waste remaining thereon is placed near the upper ice storage tank heat exchanger 30a. 3 can be achieved without freezing the whole. Therefore, for example, even when the heat storage amount is small, the ice heat storage tank 3
It is not necessary to freeze the whole, and even when it is not possible to store sufficient cold heat, the tissue cells of vegetable waste can be destroyed, and the processing performance of the wastewater treatment tank 4 at the subsequent stage can be stabilized.

【0054】図4は本発明の更に別の実施の形態による
排水処理装置の全体構成図を示す。この例は、氷蓄熱槽
3と排水処理槽4との間の解凍水貯留槽17を組み込ん
だ構成としたものである。そして、この解凍水貯留槽1
7と排水処理槽4との間の流路に排水を流量調整しつつ
搬送する排水調整ポンプ18を設け、更に解凍水貯溜槽
17には熱併給措置6に接続されて解凍水貯留槽17内
の排水温度を調整するための保温加熱用熱交換器37を
備えている。これ以外の構成は図2の例と同じである。
FIG. 4 shows an overall configuration diagram of a wastewater treatment apparatus according to still another embodiment of the present invention. This example has a configuration in which a thawed water storage tank 17 between the ice heat storage tank 3 and the wastewater treatment tank 4 is incorporated. And this thawing water storage tank 1
A drainage adjustment pump 18 is provided in the flow path between the drainage treatment tank 4 and the drainage treatment tank 4 while adjusting the flow rate of the wastewater. And a heat exchanger 37 for keeping and heating the water for adjusting the temperature of the waste water. The other configuration is the same as the example of FIG.

【0055】図4の構成において、氷蓄熱槽3で解凍処
理された排水は解凍水排出ポンプ12を介して解凍水貯
溜槽17に貯められる。このとき、排水の温度は一般的
には5〜15℃程度の低い温度であるが、後段の排水処
理槽4の浄化処理部22の処理方式が温度に影響される
生物方式等であると、5〜15℃程度の低い温度は好ま
しくない。
In the configuration shown in FIG. 4, the wastewater defrosted in the ice heat storage tank 3 is stored in the defrosted water storage tank 17 via the defrosted water discharge pump 12. At this time, the temperature of the wastewater is generally a low temperature of about 5 to 15 ° C. However, if the treatment method of the purification processing unit 22 of the subsequent wastewater treatment tank 4 is a biological method or the like affected by the temperature, Temperatures as low as 5-15 ° C are not preferred.

【0056】そこで、解凍水貯留槽17内の保温加熱用
熱交換器37を用いて、排水の温度を15〜50℃まで
加熱する。生物処理に適する温度としては25〜40℃
の範囲とすることが好ましい。
Then, the temperature of the waste water is heated to 15 to 50 ° C. by using the heat exchanger 37 for keeping heat in the thawed water storage tank 17. 25-40 ° C as temperature suitable for biological treatment
It is preferable to be within the range.

【0057】また、排水調整ポンプ18の運転制御によ
って、後段の排水処理槽4に流入する排水量を一定化す
ることで、排水処理槽4の働きの安定化を図ることがで
きる。
Further, by controlling the operation of the drainage adjusting pump 18 to stabilize the amount of wastewater flowing into the downstream wastewater treatment tank 4, the operation of the wastewater treatment tank 4 can be stabilized.

【0058】なお、解凍水貯留槽17内の加熱運転を、
冷房運転時の空調ユニット8の戻り側の冷媒の予備冷却
として、或いは、氷蓄熱槽3の凍結処理運転時の温熱排
出補助として利用すれば、解凍水貯留槽17が持つ冷熱
を余すところなく有効に利用できる。
The heating operation in the thawing water storage tank 17 is performed as follows.
If it is used as pre-cooling of the refrigerant on the return side of the air conditioning unit 8 during the cooling operation, or as auxiliary heat release during the freezing operation of the ice heat storage tank 3, the cold heat of the thawed water storage tank 17 is effectively used. Available to

【0059】[0059]

【発明の効果】請求項1に記載の発明では、組織等が破
壊された厨芥等を排水浄化するので浄化速度が速くなる
ほか、浄化度が向上すると共に水の再利用と蓄熱による
エネルギー有効利用が同時に可能となる。
According to the first aspect of the present invention, kitchen waste and the like in which tissues and the like are destroyed are subjected to wastewater purification, so that the purification speed is increased, the degree of purification is improved, and water is reused and energy is efficiently used by storing heat. Becomes possible at the same time.

【0060】請求項2に記載の発明では、上方位置には
きれいな水を集め下方位置には組織等が破壊されたペー
スト状固形物を濃縮分離させることができ、上方位置の
きれいな水を分離抽出して再利用できる。
According to the second aspect of the present invention, clean water can be collected at the upper position, and paste-like solids with broken tissue can be concentrated and separated at the lower position, and the clean water at the upper position can be separated and extracted. And can be reused.

【0061】請求項3に記載の発明では、解凍された排
水から固形物と水を効率よく分離できる。
According to the third aspect of the present invention, solids and water can be efficiently separated from the thawed wastewater.

【0062】請求項4に記載の発明では、粗濾過で残留
した厨芥等の組織破壊が効率よく行われ、排水処理槽に
おける浄化速度がいっそう速くなり、浄化度も更に向上
させることができる。
According to the fourth aspect of the present invention, tissue destruction of kitchen garbage and the like remaining by the coarse filtration is efficiently performed, the purification speed in the wastewater treatment tank is further increased, and the purification degree can be further improved.

【0063】請求項5に記載の発明では、排水処理槽に
流入する排水温度を排水処理に適した温度に調整でき、
排水処理槽の性能を安定化させることができる。
According to the fifth aspect of the present invention, the temperature of the wastewater flowing into the wastewater treatment tank can be adjusted to a temperature suitable for wastewater treatment.
The performance of the wastewater treatment tank can be stabilized.

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

【図1】本発明の一実施の形態による排水処理装置の全
体構成図
FIG. 1 is an overall configuration diagram of a wastewater treatment apparatus according to an embodiment of the present invention.

【図2】本発明の別の実施の形態よる排水処理装置の全
体構成図
FIG. 2 is an overall configuration diagram of a wastewater treatment apparatus according to another embodiment of the present invention.

【図3】図2の構成に用いる粗濾過装置の概略図FIG. 3 is a schematic diagram of a coarse filtration device used in the configuration of FIG. 2;

【図4】本発明の更に別の実施の形態による排水処理装
置の全体構成図
FIG. 4 is an overall configuration diagram of a wastewater treatment apparatus according to still another embodiment of the present invention.

【図5】特開平6−18069号公報に記載の従来の技
術を示す図
FIG. 5 is a diagram showing a conventional technique described in Japanese Patent Application Laid-Open No. 6-18069.

【図6】特開平10−73290号公報に記載の従来の
技術を示す図
FIG. 6 is a diagram showing a conventional technique described in JP-A-10-73290.

【符号の説明】[Explanation of symbols]

1 排水処理装置 2 一次貯留槽 3 氷蓄熱槽 4 排水処理槽 6 熱併給装置 8 空調ユニット 9 ディスポーザ 10 下水配管 11 排水供給ポンプ 12 解凍水排出ポンプ 13 初期融解水ポンプ 15 放水ポンプ 17 解凍水貯溜槽 18 排水調整ポンプ 19 粗濾過パネル 20 粗濾過パネル駆動部 21 濾過部 22 浄化処理部 23 沈降部 24 汚泥 25 浄化処理水 26 放水配管 30a 上方氷蓄熱槽熱交換器 30b 下方氷蓄熱槽熱交換器 32 加熱用熱交換器 37 保温加熱用熱交換器 40 電源 DESCRIPTION OF SYMBOLS 1 Wastewater treatment apparatus 2 Primary storage tank 3 Ice heat storage tank 4 Wastewater treatment tank 6 Cogeneration system 8 Air conditioning unit 9 Disposer 10 Sewage piping 11 Wastewater supply pump 12 Thawing water discharge pump 13 Initial melting water pump 15 Water discharge pump 17 Thawing water storage tank Reference Signs List 18 Drainage adjustment pump 19 Coarse filtration panel 20 Coarse filtration panel drive unit 21 Filtration unit 22 Purification treatment unit 23 Settling unit 24 Sludge 25 Purification treatment water 26 Discharge pipe 30a Upper ice storage tank heat exchanger 30b Lower ice storage tank heat exchanger 32 Heat exchanger for heating 37 Heat exchanger for insulated heating 40 Power supply

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】厨芥等を含む排水が流入する氷蓄熱槽と、 前記氷蓄熱槽内の排水に冷熱を与えて含有固形成分を凍
結速度の違いにより濃縮分離するとともにこの凍結した
排水を解凍し、この凍結操作と解凍操作により前記含有
固形物の組織を破壊することができる熱併給装置と、 解凍された排水を浄化処理する排水処理槽を備えたこと
を特徴とする排水処理装置。
1. An ice heat storage tank into which wastewater containing kitchen waste and the like flows in, and a cooling water is given to the wastewater in the ice heat storage tank to concentrate and separate solid components contained in the ice heat storage tank at different freezing speeds and to thaw the frozen wastewater. A waste heat treatment apparatus comprising: a heat and heat supply device capable of destroying the tissue of the solid content by the freezing operation and the thawing operation; and a waste water treatment tank for purifying the thawed waste water.
【請求項2】氷蓄熱槽には、排水を上方位置から下方位
置に向けて凍結させる凍結調整部が設けられていること
を特徴とする請求項1記載の排水処理装置。
2. The wastewater treatment apparatus according to claim 1, wherein the ice heat storage tank is provided with a freezing adjusting section for freezing the wastewater from an upper position to a lower position.
【請求項3】氷蓄熱槽には、解凍された排水を濾過する
ための融解水濾過部が設けられている請求項1または2
記載の排水処理装置。
3. An ice heat storage tank is provided with a molten water filtration section for filtering thawed waste water.
The wastewater treatment device as described in the above.
【請求項4】凍結調整部の下側近傍位置に粗濾過部が設
けられ、前記粗濾過部に残留した固形成分を前記粗濾過
された排水より先に前記熱併給装置により凍結させるこ
とを特徴とする請求項1記載の排水処理装置。
4. A coarse filtration unit is provided at a position near the lower side of the freezing adjustment unit, and solid components remaining in the coarse filtration unit are frozen by the cogeneration device before the coarsely filtered wastewater. The wastewater treatment device according to claim 1, wherein
【請求項5】氷蓄熱槽で分離された固形物を含んだ排水
を加熱する排水温度調整手段を備えたことを特徴とする
請求項1から4のいずれかに記載の排水処理装置。
5. The wastewater treatment apparatus according to claim 1, further comprising a wastewater temperature adjusting means for heating wastewater containing solid matter separated in the ice heat storage tank.
JP10197056A 1998-07-13 1998-07-13 Waste water discharging section Pending JP2000024643A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10197056A JP2000024643A (en) 1998-07-13 1998-07-13 Waste water discharging section

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10197056A JP2000024643A (en) 1998-07-13 1998-07-13 Waste water discharging section

Publications (1)

Publication Number Publication Date
JP2000024643A true JP2000024643A (en) 2000-01-25

Family

ID=16367989

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10197056A Pending JP2000024643A (en) 1998-07-13 1998-07-13 Waste water discharging section

Country Status (1)

Country Link
JP (1) JP2000024643A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108507083A (en) * 2018-03-05 2018-09-07 浙江理工大学 Ice-storage type heat source tower heat pump system and device and method
CN112919704A (en) * 2021-01-26 2021-06-08 江苏泰斗环保工程科技有限公司 Green treatment method of emulsion polymerization resin wastewater

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108507083A (en) * 2018-03-05 2018-09-07 浙江理工大学 Ice-storage type heat source tower heat pump system and device and method
CN112919704A (en) * 2021-01-26 2021-06-08 江苏泰斗环保工程科技有限公司 Green treatment method of emulsion polymerization resin wastewater

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