JPH0259397B2 - - Google Patents

Info

Publication number
JPH0259397B2
JPH0259397B2 JP22973684A JP22973684A JPH0259397B2 JP H0259397 B2 JPH0259397 B2 JP H0259397B2 JP 22973684 A JP22973684 A JP 22973684A JP 22973684 A JP22973684 A JP 22973684A JP H0259397 B2 JPH0259397 B2 JP H0259397B2
Authority
JP
Japan
Prior art keywords
waste
heat exchange
water
waste water
heat
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.)
Expired - Lifetime
Application number
JP22973684A
Other languages
Japanese (ja)
Other versions
JPS61107093A (en
Inventor
Itsuo Kasahara
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP59229736A priority Critical patent/JPS61107093A/en
Publication of JPS61107093A publication Critical patent/JPS61107093A/en
Publication of JPH0259397B2 publication Critical patent/JPH0259397B2/ja
Granted legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D17/00Domestic hot-water supply systems
    • F24D17/0005Domestic hot-water supply systems using recuperation of waste heat
    • F24D17/001Domestic hot-water supply systems using recuperation of waste heat with accumulation of heated water
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00Heat sources or energy sources
    • F24D2200/16Waste heat
    • F24D2200/20Sewage water
    • 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
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/18Domestic hot-water supply systems using recuperated or waste heat

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、浴場等から排出される廃湯処理装置
に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for treating waste water discharged from bathhouses and the like.

[従来の技術] 浴場等においては、廃湯を廃湯熱回収槽からな
る廃湯処理装置に導入し、そこで廃湯の熱を風呂
用水に取り込み、風呂用水を温化している。しか
し、廃湯には、毛髪、垢、石鹸やシヤンプーの泡
等の浮遊性の汚物が混入しているので、これが廃
湯熱回収槽に流入されると、該槽に設置された熱
交換器に上記汚物が付着して、熱交換率が低下
し、また廃湯の流れが悪くなるため、廃湯の熱損
失が一層大きくなる欠点があつた。さらに、熱交
換器は銅板等からなるため、上記汚物が付着する
と、熱交換器の腐食を惹起する欠点があつた。
[Prior Art] In bathhouses and the like, waste hot water is introduced into a waste water treatment device consisting of a waste water heat recovery tank, where the heat of the waste water is taken into bath water to warm the bath water. However, since waste hot water contains floating contaminants such as hair, dirt, soap and shampoo foam, when this flows into the waste water heat recovery tank, the heat exchanger installed in the tank The above-mentioned filth adheres to the water, reducing the heat exchange efficiency and impairing the flow of the waste hot water, which has the disadvantage of further increasing the heat loss of the waste hot water. Furthermore, since the heat exchanger is made of a copper plate or the like, there is a drawback that if the dirt adheres to the heat exchanger, it causes corrosion of the heat exchanger.

このため、廃湯熱回収槽は毎日清掃しなければ
ならないが、廃湯に混入された上記汚物のため清
掃時の臭気が著しく、また通常露天設置のため雨
天の時等には作業がしずらい等、清掃作業に伴な
う種々の因難があつた。
For this reason, the waste water heat recovery tank must be cleaned every day, but due to the above-mentioned filth mixed into the waste water, there is a strong odor during cleaning, and since it is usually installed in the open air, the work is slow during rainy days. There were various problems associated with cleaning work, such as leprosy.

このようなわけで、従来、廃湯熱回収槽は毎日
清掃されていない場合が多く、熱交換率の低下と
熱交換器の腐食等に悩まされていたのである。
For this reason, in the past, waste water heat recovery tanks were often not cleaned every day, resulting in problems such as a decrease in heat exchange efficiency and corrosion of the heat exchanger.

[発明が解決しようとする問題点] 本発明は、上記欠点を解決し、廃湯熱の高率回
収を図るとともに、熱交換器の腐食防止を図り、
さらに廃湯熱回収槽の清掃が簡単かつ容易に行な
える廃湯処理装置を供することを目的とする。
[Problems to be Solved by the Invention] The present invention solves the above-mentioned drawbacks, aims at high efficiency recovery of waste water heat, and aims at preventing corrosion of the heat exchanger.
Furthermore, it is an object of the present invention to provide a waste water treatment device that allows the waste water heat recovery tank to be cleaned simply and easily.

[問題点を解決するための手段] 上記目的達成のため、本発明は、流し場に連通
されるとともに底部に設けられた着脱自在の栓に
より下水溝に連通された受槽部と、該受槽部連通
された熱交換槽部とからなり、該熱交換槽部は相
互に連通する複数室に区画され、各室が底部に設
けられた着脱自在の栓により下水溝に連通され、
かつ各室に銅板等高熱伝導体からなる熱交換器が
設けられ、該熱交換器は各々相互に連通されると
ともに、一方で水源に連通され、他方で釜に連通
された廃湯熱回収槽からなる廃湯処理装置におい
て、受槽部に貫通孔を有するパイプ体からなる栓
体が着脱自在に固定され、該パイプ体が常時にお
ける廃湯の流入水位と略同一高に形成され、かつ
上記パイプ体の頂上部の廃湯流入部位に切欠が設
けられ、熱交換槽部の底部には、コンプレツサに
連結された散気体が設けられたことを特徴とする
廃湯処理装置を供する。
[Means for Solving the Problems] In order to achieve the above object, the present invention provides a receiving tank section which is connected to a sink and is also connected to a sewer ditch by a removable stopper provided at the bottom, and the receiving tank section. The heat exchange tank section is divided into a plurality of chambers that communicate with each other, and each chamber is connected to a sewer drain by a removable plug provided at the bottom.
In addition, each chamber is provided with a heat exchanger made of a high heat conductor such as a copper plate, and the heat exchangers are connected to each other, and a waste water heat recovery tank is connected to a water source on one side and a boiler on the other side. In a waste water treatment device, a plug body made of a pipe body having a through hole is removably fixed to the receiving tank part, the pipe body is formed at approximately the same height as the inflow water level of the waste hot water at all times, and the pipe body A waste hot water treatment device is provided, characterized in that a notch is provided at the waste hot water inflow site at the top of the body, and a gas diffuser connected to a compressor is provided at the bottom of the heat exchange tank.

[実施例] 本発明にかかる廃湯処理装置を図面に示す実施
例に基ずいて設明する。
[Example] A waste hot water treatment apparatus according to the present invention will be constructed based on an example shown in the drawings.

廃湯熱回収槽1からなる廃湯処理装置は、上部
が開放された直方体の槽であり、一端部に固定の
または着脱自在の仕切り板2により仕切られた受
槽部3が形成され、残部に熱交換槽部4が形成さ
れる。上記受槽部3は、廃湯溝5により流し場6
に連通され、底部に設けられた着脱自在の栓体7
により下水溝8に連通される。該下水溝8は、街
の下水管(図示せず)に連通される。上記栓体7
は、貫通孔9を有するパイプ体10からなり、下
部にゴム11が巻着されて受槽部3の底部に着脱
自在に固定される。上記パイプ体10は、常時に
おける廃湯の流入水位lと略同一高に形成されて
いるので、栓体7は受槽部3の底部に固定される
と、廃湯の流入水位より若干下方に位置される。
上記パイプ体10の頂上部には、廃湯の流入部位
に切欠12が設けられる。該切欠12は、適宜の
形状に形成されるが、U字状に形成されるのが廃
湯の吸込みを良くする上で望ましい。13は上記
栓体7の着脱自在時に使用される金棒である。
The waste water treatment device consisting of the waste water heat recovery tank 1 is a rectangular parallelepiped tank with an open top, and a receiving tank part 3 partitioned by a fixed or removable partition plate 2 is formed at one end, and the remaining part is a rectangular parallelepiped tank with an open top. A heat exchange tank section 4 is formed. The receiving tank 3 is connected to a sink 6 by a waste water groove 5.
A removable stopper 7 provided at the bottom of the
It is communicated with the sewer ditch 8 by. The sewer 8 is connected to a city sewer pipe (not shown). The above plug body 7
consists of a pipe body 10 having a through hole 9, a rubber 11 is wrapped around the lower part, and the pipe body 10 is removably fixed to the bottom of the receiving tank part 3. The pipe body 10 is formed at approximately the same height as the inflow water level l of waste hot water at all times, so when the plug body 7 is fixed to the bottom of the receiving tank 3, it is located slightly below the inflow water level of waste hot water. be done.
A notch 12 is provided at the top of the pipe body 10 at an inflow site for waste hot water. The notch 12 may be formed in any suitable shape, but it is preferable to form it in a U-shape in order to improve suction of waste hot water. Reference numeral 13 denotes a metal rod used when the plug body 7 is detachable.

熱交換部4は、上記仕切り板2により上記受槽
部3に隣接して形成され、かつ該仕切り板2の下
部に設けられた開口により該受槽部3に連通され
る。上記熱交換槽部4は、固定のまたは着脱自在
の仕切り板2a,2b,…2r,2s、2tによ
り複数室(本例では20室)4a,4b,4c…4
r,4s,4tに区画される。各室は底部に設け
られた着脱自在の栓14a,14b,14c…1
4r,14s,14tにより下水溝8に連通され
る。浮遊性の汚物が多いときには、熱交換槽部の
第一室4aに設けられる栓14aは、上記栓体7
と同様、常時における廃湯の流入水位lと略同一
高に形成された貫通孔を有するパイプ体からなる
もの(図示省略)が望ましい。この場合のパイプ
体は、上記栓体7より小径であり、また上記栓体
7にある切欠12がなくともよい。熱交換槽部の
各室4a,4b,4c…4r,4s,4tには熱
交換器15a,15b,…15r,15s,15
tが設けられる。該熱交換器15a,15b,…
15r,15s,15tは、仕切り板2a,2
b,…2r、2s,2tに付設された密閉の中空
箱体であり、6面が銅板またはステンレス板のよ
うな高熱伝導体からなる。該熱交換器は、各々内
部に廃湯を通す適宜数の廃湯管16が上下に開口
されて設けられる。上記熱交換換器15の上部に
は、風呂用水を通す連通管17が交互に連結さ
れ、これにより熱交換器15a,15b,…15
r,15s,15t相互が連通されている。そし
て、最後室の熱交換器15tが井水等の水源18
に連通され、第一室の熱交換器15aが釜19に
連通される。上記熱交換槽部4の底部には、コン
プレツサ20に連結された散気体21が敷設され
る。該散気体21は、細小な気泡を生ずるもので
あれば、パイプ状のものでも面状のものでもよ
い。22は廃湯熱回収槽1の他端に設けられた流
出槽部、23は該流出槽部の端壁上部中央に設け
られた廃湯流出用の切込部である。該流出槽部2
2は、熱交換器を設けて熱交換槽部に形成しても
よい。24は、流し場6の廃湯溝5の最も上の溝
の入口に載置された汚物処理用のバクテリアから
なる処理剤である。
The heat exchange section 4 is formed adjacent to the receiving tank section 3 by the partition plate 2, and is communicated with the receiving tank section 3 through an opening provided at the lower part of the partition plate 2. The heat exchange tank section 4 has a plurality of rooms (20 rooms in this example) 4a, 4b, 4c, .
It is divided into r, 4s, and 4t. Each chamber has removable plugs 14a, 14b, 14c...1 provided at the bottom.
4r, 14s, and 14t communicate with the sewer ditch 8. When there is a large amount of floating waste, the plug 14a provided in the first chamber 4a of the heat exchange tank section is closed to the plug 7.
Similarly, it is preferable to use a pipe body (not shown) having a through hole formed at approximately the same height as the inflow water level l of the waste hot water at all times. The pipe body in this case has a smaller diameter than the plug body 7, and the notch 12 in the plug body 7 may not be provided. Heat exchangers 15a, 15b,...15r, 15s, 15 are installed in each chamber 4a, 4b, 4c...4r, 4s, 4t of the heat exchange tank section.
t is provided. The heat exchangers 15a, 15b,...
15r, 15s, 15t are partition plates 2a, 2
b,...2r, 2s, 2t are sealed hollow boxes, and six sides are made of a high heat conductor such as a copper plate or a stainless steel plate. The heat exchanger is provided with an appropriate number of waste hot water pipes 16 that are open at the top and bottom, each through which waste hot water passes. Communication pipes 17 for passing bath water are connected alternately to the upper part of the heat exchanger 15, and thereby the heat exchangers 15a, 15b,...15
r, 15s, and 15t are in communication with each other. The heat exchanger 15t in the last chamber is connected to a water source 18 such as well water.
The heat exchanger 15a in the first chamber is communicated with the pot 19. At the bottom of the heat exchange tank section 4, a gas diffuser 21 connected to a compressor 20 is installed. The gas diffuser 21 may be pipe-shaped or planar as long as it generates small bubbles. Reference numeral 22 designates an outflow tank portion provided at the other end of the waste water heat recovery tank 1, and 23 designates a notch portion for outflowing the waste water provided at the center of the upper part of the end wall of the outflow tank portion. The outflow tank part 2
2 may be formed in the heat exchange tank section by providing a heat exchanger. Reference numeral 24 denotes a treatment agent made of bacteria for waste treatment placed at the entrance of the uppermost groove of the waste water groove 5 of the sink 6.

[作用] 次に、本発明にかかる廃湯処理装置の作用につ
いて説明する。
[Function] Next, the function of the waste water treatment device according to the present invention will be explained.

まず、営業終了後、流し場6および浴槽の清掃
前に栓体7を抜いておく。栓体7には金棒13が
付設されているから、遠隔からの着脱操作が容易
である。次いで、流し場6等を清掃すると、清掃
時に使用されるクレンザー等の研磨剤が直接受槽
部3より下水溝8に流せるので、研磨剤が熱交換
槽部4に流れ込まない。研磨剤は、熱交換器15
を損傷させるので、できるだけ熱交換槽部4への
流入を回避させるべきであるが、従来は受槽部の
栓を抜かないで清掃していたため、研磨剤が混入
された廃湯が熱交換槽部に流れ込んで熱交換器1
5を損傷させていたのである。清掃中は熱交換槽
部4各室の栓14a,14b,14c…14r,
14s,14tも各々抜いて、各室の冷たくなつ
た廃湯を下水溝8に流しておくのが望ましい。こ
の場合においても、各栓14a,14b,14c
…14r,14s,14tには金棒13が付設さ
れているから、遠隔からの着脱操作が容易であ
る。清掃が終了したら、流し場6の廃湯溝5の最
も上の溝の入口に汚物処理用のバクテリアからな
る処理剤24を載置し、また受槽部3に栓体7を
嵌合し、熱交換槽部4各室の栓14a〜14tを
嵌合する。
First, after business hours are over, the stopper 7 is removed before cleaning the sink 6 and bathtub. Since a metal rod 13 is attached to the plug body 7, it is easy to attach and detach it remotely. Next, when the sink 6 and the like are cleaned, the abrasive such as a cleanser used during cleaning can flow directly from the receiving tank 3 to the drain 8, so that the abrasive does not flow into the heat exchange tank 4. The abrasive is transferred to the heat exchanger 15
The flow into the heat exchange tank 4 should be avoided as much as possible, as it may damage the water, but in the past, cleaning was done without removing the stopper from the receiving tank, so waste water mixed with abrasives could flow into the heat exchange tank 4. into heat exchanger 1
5 was damaged. During cleaning, the plugs 14a, 14b, 14c...14r,
14s and 14t are also drained, and it is desirable to drain the cold waste water from each room into the drain 8. Also in this case, each stopper 14a, 14b, 14c
... Since the metal rods 13 are attached to 14r, 14s, and 14t, it is easy to attach and detach them remotely. After the cleaning is completed, a treatment agent 24 made of bacteria for filth treatment is placed at the entrance of the uppermost groove of the waste water groove 5 of the sink 6, and the stopper 7 is fitted into the receiving tank 3, and heated. The plugs 14a to 14t of each chamber of the exchange tank section 4 are fitted.

しかして、営業する。営業中においては、廃湯
溝5から多量の廃湯が受槽部3に流入してくる。
この廃湯には、毛髪、垢、石鹸やシヤンプーの泡
等の浮遊性の汚物が混入されており、かかる浮遊
性の汚物が廃湯の上に乗つて流れてくる。このと
き、受槽部3には、栓体7が廃湯の流入水位より
若干下方に位置するよう固定されており、かつ該
栓体7は頂上部の廃湯流入部位に切欠12が設け
られているので、上記浮遊性の汚物は一部の廃湯
に乗つたまま上記切欠12から栓体7の貫通孔9
内に流れ込み、該貫通孔9を通つて直接下水溝8
に流出する。したがつて、熱交換槽部4には、上
記浮遊性の汚物は殆ど流入されない。
However, I am open for business. During business hours, a large amount of waste hot water flows into the receiving tank 3 from the waste hot water groove 5.
This waste water contains floating filth such as hair, grime, soap and shampoo foam, and the floating filth floats on top of the waste water. At this time, a stopper 7 is fixed to the receiving tank 3 so as to be located slightly below the inflow level of the waste hot water, and the stopper 7 is provided with a notch 12 at the waste water inflow site at the top. Therefore, the floating waste flows from the notch 12 to the through hole 9 of the plug body 7 while remaining on some of the waste water.
into the sewer drain 8 directly through the through hole 9.
leaks to. Therefore, almost no floating filth flows into the heat exchange tank section 4.

受槽部3に流入した廃湯は、仕切り板2の下部
に設けられた開口から熱交換槽部第一室4aに流
入する。焼交換槽部第一室4aに流入した廃湯
は、流圧によつて上方に押し上げられ、廃湯管1
6の上方の口から熱交換器15a内に流入し、廃
湯管16を通つて下方の口から流出し、仕切り板
2aの下方に設けられた開口から熱交換槽部第二
室4bに流入する。上記の場合において、熱交換
槽部第一室4aに前記したようなパイプ体からな
る栓体が固定されていれば、該第一室4aに流入
した浮遊性汚物の残部を殆ど一部の廃湯とともに
栓体の貫通孔から直接下水溝8に放流することが
できる。かようにして、一連の熱交換槽部4を通
過した廃湯は、廃湯熱回収槽1の他端に設けられ
た切込部23から溢出し下水溝8に流出する。
The waste hot water that has flowed into the receiving tank section 3 flows into the first chamber 4a of the heat exchange tank section through an opening provided at the lower part of the partition plate 2. The waste hot water that has flowed into the first chamber 4a of the sintering exchange tank section is pushed upward by the flow pressure and flows into the waste hot water pipe 1.
6 flows into the heat exchanger 15a from the upper opening, flows out through the lower opening through the waste pipe 16, and flows into the heat exchange tank second chamber 4b from the opening provided below the partition plate 2a. do. In the above case, if a stopper made of a pipe as described above is fixed to the first chamber 4a of the heat exchange tank part, most of the remaining floating waste that has flowed into the first chamber 4a can be removed. The hot water can be discharged directly into the drain 8 from the through hole of the stopper. In this way, the waste hot water that has passed through the series of heat exchange tank sections 4 overflows from the notch 23 provided at the other end of the waste water heat recovery tank 1 and flows into the sewage groove 8.

しかして、かかる熱交換槽部4においては、上
記のように、浮遊性の汚物が殆ど流入されないか
ら、熱交換器15にはかかる汚物が付着されな
い。しかも、熱交換槽部4の各室では、コンプレ
ツサ20から供給されたエアが散気体21より細
小な気泡となつて吐出されているので、熱交換器
15への汚物の付着は一層防止される。この結
果、廃湯熱が高率で回収されるとともに、熱交換
器の腐食が防止されるのである。
Therefore, as described above, almost no floating filth flows into the heat exchange tank section 4, so that such filth does not adhere to the heat exchanger 15. Moreover, in each chamber of the heat exchange tank section 4, the air supplied from the compressor 20 is discharged from the gas diffuser 21 in the form of fine bubbles, so that the adhesion of dirt to the heat exchanger 15 is further prevented. . As a result, waste water heat is recovered at a high rate and corrosion of the heat exchanger is prevented.

即ち、熱交換槽部4の各室において散気体21
よりエアが供給されと、このエアの供給圧と気泡
の上昇力によつて、廃湯の流れが促進される。熱
交換槽部第一室4aに流入される廃湯の温度は、
38℃程度であるが、これが熱交換槽部最後室4t
から流出されるとき、従来は19℃程度にまで低下
していたが、本願発明においては廃湯の流れが促
進される結果、本実施例では25℃程度の湯温を維
持した。また、気泡が熱交換器15の界面で破裂
するときの力により、熱交換器15の表面に付着
された汚物が剥離され、かつ上記表面への汚物の
付着が防止される。さらに、廃湯は廃湯溝5の入
口に載置された汚物処理用のバクテリアからなる
処理剤24を通過してくるため、熱交換槽部4へ
流入される廃湯にはバクテリアが混入されている
が、上記エアの供給はこのバクテリアへの有効な
酸素補給となり、バクテリアが一層活性化され、
熱交換槽部4へ一部流入された汚物が分解される
ことにより、廃湯の浄化が一層促進されるのであ
る。
That is, in each chamber of the heat exchange tank section 4, the gas diffuser 21
When more air is supplied, the flow of waste hot water is promoted by the supply pressure of the air and the upward force of the bubbles. The temperature of the waste hot water flowing into the first chamber 4a of the heat exchange tank section is:
The temperature is about 38℃, and this is the 4t last chamber of the heat exchange tank.
Conventionally, the temperature of the waste hot water would drop to about 19°C when it was discharged from the water, but as a result of the present invention promoting the flow of waste hot water, the temperature of the hot water was maintained at about 25°C in this example. In addition, the force generated when the bubble bursts at the interface of the heat exchanger 15 peels off dirt adhering to the surface of the heat exchanger 15, and prevents dirt from adhering to the surface. Furthermore, since the waste hot water passes through a treatment agent 24 made of bacteria for filth treatment placed at the entrance of the waste water groove 5, bacteria are mixed into the waste hot water flowing into the heat exchange tank section 4. However, the above air supply effectively supplies oxygen to the bacteria, further activating the bacteria.
By decomposing some of the waste that has flowed into the heat exchange tank section 4, purification of the waste hot water is further promoted.

この結果、廃湯の熱損失が低減され、廃湯熱の
風呂用水への熱交換効率が増大されるのである。
即ち、熱交換槽部4に設けられた熱交換器15に
は、上記廃湯の流れとは反対方向に水源18より
風呂用水が流入され、各熱交換器15を通過する
とき上記廃湯の熱が風呂用水に伝導され、これが
温化されるのであるが、約17℃の風呂用水が(井
水の場合)が熱交換槽部第一室4aを通過すると
きの温度は、従来27℃程度であつたが、本実施例
では35℃程度に上昇した。また、浮遊性汚物の付
着が防止される結果、熱交換器の腐食が防止され
るのである。
As a result, the heat loss of waste water is reduced, and the efficiency of heat exchange of waste water heat to bath water is increased.
That is, bath water flows into the heat exchanger 15 provided in the heat exchange tank 4 from the water source 18 in the opposite direction to the flow of the waste hot water, and as it passes through each heat exchanger 15, the waste water flows. Heat is conducted to the bath water, which warms it. Conventionally, the temperature of bath water (in the case of well water) of about 17°C when it passes through the first chamber 4a of the heat exchange tank is 27°C. However, in this example, the temperature rose to about 35°C. Furthermore, as the adhesion of floating dirt is prevented, corrosion of the heat exchanger is prevented.

[発明の効果] このように、本発明にかかる廃湯処理装置によ
れば、熱交換槽部に汚物が殆ど流入せず、一部流
入する汚物も熱交換器への付着を略完全に防止で
きるから、廃湯熱を高率で回収することができ、
また、熱交換器の腐食を防止することができる。
さらに、廃湯熱回収槽は、営業中即ち廃湯と風呂
用水との熱交換中に、汚物が処理されているか
ら、廃湯熱回収槽の清掃は、少なくとも受槽部の
栓体を操作するだけでよく、非常に簡単かつ容易
に行なうことができる。
[Effects of the Invention] As described above, according to the waste water treatment apparatus according to the present invention, almost no filth flows into the heat exchange tank, and even the filth that partially flows into the heat exchanger is almost completely prevented from adhering to the heat exchanger. Because it is possible to recover waste water heat at a high rate,
Furthermore, corrosion of the heat exchanger can be prevented.
Furthermore, since the waste water heat recovery tank is treated with waste during its operation, that is, during the heat exchange between waste water and bath water, cleaning the waste water heat recovery tank requires at least operating the stopper of the receiving tank. It's very simple and easy to do.

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

図面は本発明にかかる廃湯処理装置の実施例を
示し、第1図はその正面断面図、第2図は一部省
略平面図、第3図は栓体の拡大斜示図である。 1……廃湯熱回収槽、3……受槽部、4……熱
交換槽部、6……流し場、7……栓体、8……下
水溝、9……貫通孔、10……パイプ体、12…
…切欠、15……熱交換器、17……連通管、1
8……水源、19……釜、21……散気体。
The drawings show an embodiment of the waste water treatment apparatus according to the present invention, and FIG. 1 is a front sectional view thereof, FIG. 2 is a partially omitted plan view, and FIG. 3 is an enlarged perspective view of a plug body. 1...Waste water heat recovery tank, 3...Receiving tank section, 4...Heat exchange tank section, 6...Sink area, 7...Blug body, 8...Sewage gutter, 9...Through hole, 10... Pipe body, 12...
... Notch, 15 ... Heat exchanger, 17 ... Communication pipe, 1
8... Water source, 19... Pot, 21... Gas diffuser.

Claims (1)

【特許請求の範囲】[Claims] 1 流し場に連通されるとともに底部に設けられ
た着脱自在の栓により下水溝に連通された受槽部
と、該受槽部に連通された熱交換槽部とからな
り、該熱交換槽部は相互に連通する複数室に区画
され、各室が底部に設けられた着脱自在の栓によ
り下水溝に連通され、かつ各室に銅板等高熱伝導
体からなる熱交換器が設けられ、該熱交換器は
各々相互に連通されるとともに、一方で水源に連
通され、他方で釜に連通された廃湯熱回収槽から
なる廃湯処理装置において、受槽部に貫通孔を有
するパイプ体からなる栓体が着脱自在に固定さ
れ、該パイプ体が常時における廃湯の流入水位と
略同一高に形成され、かつ上記パイプ体の頂上部
の廃湯流入部位に切欠が設けられ、熱交換槽部の
底部には、コンプレツサに連結された散気体が設
けられたことを特徴とする廃湯処理装置。
1 Consists of a receiving tank part that communicates with the sink and the sewer through a removable plug provided at the bottom, and a heat exchange tank part that communicates with the receiving tank part, and the heat exchange tank parts are mutually connected. Each chamber is divided into a plurality of chambers that communicate with each other, each chamber is connected to a sewer drain through a removable stopper provided at the bottom, and each chamber is equipped with a heat exchanger made of a highly thermally conductive material such as a copper plate. In a waste water treatment device consisting of a waste water heat recovery tank which is connected to each other, one side is connected to a water source, and the other side is connected to a pot, a stopper body consisting of a pipe body having a through hole in the receiving tank part is provided. The pipe body is removably fixed, the pipe body is formed at approximately the same height as the inflow water level of the waste hot water at all times, and a notch is provided at the waste water inflow portion at the top of the pipe body, and a cutout is provided at the bottom of the heat exchange tank portion. is a waste water treatment device characterized by being provided with a gas diffuser connected to a compressor.
JP59229736A 1984-10-31 1984-10-31 Method of treating waste hot water and apparatus therefor Granted JPS61107093A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59229736A JPS61107093A (en) 1984-10-31 1984-10-31 Method of treating waste hot water and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59229736A JPS61107093A (en) 1984-10-31 1984-10-31 Method of treating waste hot water and apparatus therefor

Publications (2)

Publication Number Publication Date
JPS61107093A JPS61107093A (en) 1986-05-24
JPH0259397B2 true JPH0259397B2 (en) 1990-12-12

Family

ID=16896880

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59229736A Granted JPS61107093A (en) 1984-10-31 1984-10-31 Method of treating waste hot water and apparatus therefor

Country Status (1)

Country Link
JP (1) JPS61107093A (en)

Also Published As

Publication number Publication date
JPS61107093A (en) 1986-05-24

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