JPH08128726A - Waste water heat recovery system - Google Patents
Waste water heat recovery systemInfo
- Publication number
- JPH08128726A JPH08128726A JP26773594A JP26773594A JPH08128726A JP H08128726 A JPH08128726 A JP H08128726A JP 26773594 A JP26773594 A JP 26773594A JP 26773594 A JP26773594 A JP 26773594A JP H08128726 A JPH08128726 A JP H08128726A
- Authority
- JP
- Japan
- Prior art keywords
- water
- hot
- waste
- heat recovery
- wastewater
- 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
Links
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、公衆浴場等に設備され
る廃湯熱回収システムに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste water heat recovery system installed in public baths and the like.
【0002】[0002]
【従来の技術】図3は、公衆浴場に設備されている廃湯
熱回収システムであって、貯水槽1から熱源機2に至る
給水ライン3と洗い場4からの廃湯ライン5は、途中で
廃湯熱回収器(熱交換器)6で交差させることにより、
給水ライン3を流れる水に廃湯熱を与える構成であっ
て、前記廃湯熱回収器6は、図4に示すような木枠7の
中に給水ライン3を通し、この給水ライン3に取り付け
た金属板(プレート)8で伝熱面積を確保する構成であ
る。そして、上記従来の廃湯熱回収器6は、通常床下又
は地中に設置される例が多く、熱交換時の総括熱伝達係
数は100[kcal/℃・m2 hr]程度である。2. Description of the Related Art FIG. 3 shows a waste water heat recovery system installed in a public bath, in which a water supply line 3 from a water tank 1 to a heat source device 2 and a waste water line 5 from a washing place 4 are provided on the way. By crossing with the waste water heat recovery device (heat exchanger) 6,
The waste water heat recovery device 6 is configured to give heat to waste water to the water flowing through the water supply line 3, and the waste water heat recovery device 6 is attached to the water supply line 3 by passing the water supply line 3 through a wooden frame 7 as shown in FIG. The heat transfer area is secured by the metal plate (plate) 8. The conventional waste water heat recovery device 6 is usually installed under the floor or underground, and the overall heat transfer coefficient during heat exchange is about 100 [kcal / ° C · m 2 hr].
【0003】[0003]
【発明が解決しようとする課題】しかし、上記従来の廃
湯熱回収システムにおいては、次のような欠点がある。 a.総括熱伝達係数が非常に小さいため、この係数を高
めるためには、廃湯熱回収器6の寸法を大きくする必要
があり、地面への放熱面積が大きくなってしまう。 b.廃湯熱が持つ熱量のうち、50%以下しか回収され
ないのが現状である。 c.廃湯熱を有効に回収するためには、給水と廃湯が同
時にほぼ等流量で流れる必要がある。ところが、従来の
構成では、給水量に比較して廃湯量が多く、排熱損失と
して無駄に排出してしまったり、また逆に、廃湯量が少
ない時に給水量が多く流れてしまうことがある。また、
運転例によっては、どちらか一方のみ流れ、熱交換が行
われないこともある。 d.熱交換時の総括熱伝達係数は、前記のとおり100
[kcal/℃・m2 hr]程度であり、非常に小さい。However, the above-mentioned conventional waste water heat recovery system has the following drawbacks. a. Since the overall heat transfer coefficient is very small, it is necessary to increase the size of the waste water heat recovery device 6 in order to increase this coefficient, and the heat dissipation area to the ground becomes large. b. Currently, only 50% or less of the heat quantity of waste water heat is recovered. c. In order to effectively recover the heat of the waste water, it is necessary that the water supply and the waste water simultaneously flow at substantially the same flow rate. However, in the conventional configuration, the amount of waste water is large compared to the amount of water supply, and waste water is discharged as waste heat loss, or conversely, the amount of water supply may flow when the amount of waste water is small. Also,
Depending on the operation example, only one of them may flow and heat exchange may not be performed. d. The overall heat transfer coefficient during heat exchange is 100 as described above.
It is about [kcal / ℃ ・ m 2 hr], which is very small.
【0004】[0004]
【課題を解決するための手段】本発明は、上記した課題
を解決するのが目的であって、その構成は次のとおりで
ある。 1.貯水槽から廃湯熱回収器を経由して熱源機に至る給
水ラインに流量制御バルブを取り付けたこと、前記熱源
機で加熱された温水を貯湯する貯湯槽内に複数の水位を
検出するための貯湯水位センサを取り付けたこと、廃湯
を一旦廃湯槽内に溜めてから廃湯ポンプを利用して汲み
揚げ、これを前記廃湯熱回収器を経由して排水するよう
に構成したこと、前記貯湯水位センサで検出される水位
に合わせて前記流量制御バルブを制御し、且つこの流量
制御バルブで制御される水量の70〜100%の廃湯を
廃湯槽内から汲み揚げて廃湯熱回収器内に送り込むよう
に、前記廃湯ポンプを制御する制御器を設けたこと、を
特徴とする廃湯熱回収システム。 2.前記1において、廃湯槽内に水位センサを取り付け
て廃湯槽内の水位を検出し、この水位が規定以下に下っ
た場合には廃湯ポンプでの汲み揚げを停止し、規定水位
以上に上昇した場合には貯湯槽内の水位とは関係なく汲
み揚げを行ってオーバーフローしないように制御する安
全回路を設けて成る廃湯熱回収システム。 3.前記1又は2において、廃湯熱回収器としてプレー
ト式熱交換器を用いて成る廃湯熱回収システム。SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems, and the constitution thereof is as follows. 1. A flow control valve was attached to the water supply line from the water storage tank to the heat source device via the waste water heat recovery device, and for detecting multiple water levels in the hot water tank that stores hot water heated by the heat source device. A hot water storage water level sensor is attached, the waste water is temporarily stored in the waste water tank and then pumped up using a waste water pump, and is drained via the waste water heat recovery device. The waste water heat recovery device controls the flow rate control valve in accordance with the water level detected by the hot water storage water level sensor, and pumps up 70 to 100% of the waste water volume controlled by the flow rate control valve from the waste hot water tank. A waste hot water heat recovery system, characterized in that a controller for controlling the waste hot water pump is provided so as to be fed into the waste hot water heat recovery system. 2. In 1 above, a water level sensor is installed in the waste water tank to detect the water level in the waste water tank, and when the water level falls below a specified level, pumping by the waste water pump is stopped and the water level rises above the specified water level. In some cases, the waste water heat recovery system is equipped with a safety circuit that controls pumping to prevent overflow, regardless of the water level in the hot water storage tank. 3. 2. The waste hot water heat recovery system according to 1 or 2 above, which uses a plate heat exchanger as the waste hot water heat recovery device.
【0005】[0005]
【作用】貯湯槽内の水位が例えば低水位まで低下した場
合、制御器は流量制御バルブを最大に開いて給水を行
う。同時に、廃湯ポンプを最大に駆動して汲み揚げる廃
湯量を最多に制御する。この制御例を表1に示す。When the water level in the hot water storage tank drops to, for example, a low water level, the controller opens the flow control valve to the maximum to supply water. At the same time, the waste water pump is maximally driven to control the maximum amount of waste water pumped up. Table 1 shows an example of this control.
【0006】[0006]
【表1】 [Table 1]
【0007】洗い場からの廃湯は、その都度一定しない
ので、この廃湯は一旦廃湯槽に溜められ、そこから廃湯
ポンプにより汲み揚げられて排水される。給水ラインを
流れる水と、廃湯ラインを流れる廃湯は、廃湯熱回収器
で交差し、廃湯側から給水側に熱移動が行われ、給水は
昇温する。この昇温した水が熱源機に至り、加熱され、
例えば一旦貯湯槽に溜められ、ここから浴槽或いは洗い
場の蛇口に給湯される。上記制御において、廃湯熱回収
器を通過する給水量に対して70〜100%の比になる
ように廃湯ポンプは制御される。また、制御器は、熱源
機が駆動していないとき(給水がないとき)は、廃湯ポ
ンプを一旦止めて廃湯を廃湯槽内に溜めておき、熱回収
されずに廃湯してしまうのを防止する。但し、廃湯槽内
の水位センサが規定以下の水量を検出している場合には
廃湯ポンプを停止し、以上の場合には、廃湯ポンプを駆
動してオーバーフロー防止のための制御を行う。Since the waste water from the washing place is not constant each time, the waste water is temporarily stored in the waste water tank, and is then pumped up by the waste water pump and discharged. The water flowing through the water supply line and the waste water flowing through the waste water line intersect at the waste water heat recovery device, heat is transferred from the waste water side to the water supply side, and the temperature of the water supply rises. This heated water reaches the heat source machine and is heated,
For example, the water is once stored in a hot water storage tank, and hot water is supplied from here to the faucet of the bathtub or the washing area. In the above control, the waste water pump is controlled so as to have a ratio of 70 to 100% with respect to the amount of water supplied through the waste water heat recovery device. Further, when the heat source device is not driven (when there is no water supply), the controller temporarily stops the waste water pump and stores the waste water in the waste water tank, and waste heat is not recovered. Prevent. However, the waste water pump is stopped when the water level sensor in the waste water tank detects the amount of water below the regulation, and in the above cases, the waste water pump is driven to perform control for overflow prevention.
【0008】[0008]
【実施例】図1は本発明の実施例であって、1は貯水
槽、2は熱源機、3は給水ライン、4は洗い場、5、5
aは廃湯ライン、6は廃湯熱回収器(プレート式熱交換
器)、9は貯湯槽、10は貯湯槽9に取り付けられた貯
湯水位センサであって、このセンサ10は高・中・低の
3段階の水位の検出が可能である。11は廃湯ライン5
からの廃湯を一旦溜めるための廃湯槽、12はこの一旦
溜めた廃湯を前記廃湯熱回収器6を経由して廃湯するた
めの廃湯ポンプ、13は廃湯槽11に取り付けられた水
位センサ、14は給水ライン3に取り付けられた制御バ
ルブであって、この制御バルブ14は全開・中開・小開
の3段階制御が可能である。15は制御器である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an embodiment of the present invention, in which 1 is a water tank, 2 is a heat source device, 3 is a water supply line, 4 is a washing place, and 5 and 5.
a is a waste hot water line, 6 is a waste hot water heat recovery device (plate type heat exchanger), 9 is a hot water storage tank, and 10 is a hot water storage water level sensor attached to the hot water storage tank 9. It is possible to detect water levels at three low levels. 11 is waste water line 5
A waste water tank for temporarily collecting the waste hot water from the above, a waste water pump 12 for discharging the once stored waste hot water through the waste hot water heat recovery device 6, and a reference numeral 13 attached to the waste hot water tank 11. A water level sensor 14 is a control valve attached to the water supply line 3, and the control valve 14 can perform three-stage control of full open, medium open, and small open. Reference numeral 15 is a controller.
【0009】貯湯槽1の水位は貯湯水位センサ10で検
出されており、この検出される水位が低の場合、制御器
15は制御バルブ14を全開に制御し、同時に廃湯ポン
プ12を最大で駆動し、水位が中の場合は制御バルブ1
4中・廃湯ポンプ12中・高水位の場合は制御バルブ1
4小開・廃湯ポンプ12を低に制御する。洗い場4から
の廃湯は、一旦廃湯槽11に溜められ、そこから廃湯ポ
ンプ12により汲み揚げられて廃湯ライン5aから排水
される。給水ライン3を流れる水と、廃湯ライン5aを
流れる廃湯は、廃湯熱回収器6で交差し、廃湯側から給
水側に熱移動が行われ、給水は昇温する。この昇温した
水が熱源機2に至り、加熱され、一旦貯湯槽9に溜めら
れ、ここから浴槽或いは洗い場の蛇口に給湯される。The water level in the hot water storage tank 1 is detected by the hot water level sensor 10, and when the detected water level is low, the controller 15 controls the control valve 14 to be fully opened, and at the same time, the waste water pump 12 is set to the maximum. Control valve 1 when driven and the water level is medium
4 Medium / waste water pump 12 Medium / high water level control valve 1
4 Small opening / waste water pump 12 is controlled to low. The waste hot water from the washing place 4 is temporarily stored in the waste hot water tank 11, is then pumped up by the waste hot water pump 12, and is drained from the waste hot water line 5a. The water flowing through the water supply line 3 and the waste hot water flowing through the waste hot water line 5a intersect at the waste hot water heat recovery device 6, heat is transferred from the waste hot water side to the water supply side, and the temperature of the water supply rises. The heated water reaches the heat source device 2, is heated, is temporarily stored in the hot water storage tank 9, and is supplied to the faucet of the bathtub or the washing place from here.
【0010】上記給水及び廃湯の流れにおいて、給湯ラ
イン3を流れる水量に対して廃湯ライン5を流れる量は
3段階とも70〜100%に制御されている。次に、制
御器15は給水ライン3に流れがない場合は、廃湯ポン
プ12を一旦止めて廃湯を廃湯槽11内に溜めておき、
熱回収せずに廃湯してしまうのを防止する。但し、廃湯
槽11内の水位センサ13が規定水位以下を検出してい
る場合には、廃湯ポンプ12を一旦停止し、規定以上の
場合は、給水の有無に関係なく、廃湯ポンプ12を駆動
してオーバーフローするのを防止する。図2は廃湯熱回
収器6として利用したプレート式熱交換器の例であっ
て、6aはプレートフィン、6bは給水出入口、6cは
廃湯出入口である。In the above-mentioned water supply and waste water flows, the amount of water flowing through the waste water line 5 is controlled to 70 to 100% in all three levels with respect to the amount of water flowing through the hot water supply line 3. Next, when there is no flow in the water supply line 3, the controller 15 temporarily stops the waste water pump 12 and stores the waste water in the waste water tank 11.
Prevent waste water from being recovered without recovering heat. However, when the water level sensor 13 in the waste water tank 11 detects the water level below the specified level, the waste water pump 12 is temporarily stopped. Drive to prevent overflow. FIG. 2 shows an example of a plate heat exchanger used as the waste hot water heat recovery device 6, in which 6a is a plate fin, 6b is a feed water inlet / outlet, and 6c is a waste hot water inlet / outlet.
【0011】[0011]
【発明の効果】本発明の効果は次のとおりである。 a.給水と廃湯が廃湯熱回収器中を同時に流れるため、
廃湯熱回収率を70%以上に上げることが可能となる。 b.プレート式熱交換器を使うことにより、総括熱伝達
係数を従来の10倍以上の3000[kcal/℃・m2 h
r]程度まで上げられる。 c.従来型より、効率の高いシステムを用いることによ
り、省エネルギーでかつ地球に優しいシステムを構築す
ることができる。 d.給水量を給水メータで計測することにより、精度の
高い水量計測が可能となる。The effects of the present invention are as follows. a. Since the water supply and waste water flow in the waste water heat recovery device at the same time,
It is possible to raise the waste water heat recovery rate to 70% or more. b. By using a plate heat exchanger, the overall heat transfer coefficient is 3000 times more than that of the conventional model, 3000 [kcal / ℃ ・ m 2 h
r]. c. By using a system with higher efficiency than the conventional type, it is possible to construct an energy-saving and earth-friendly system. d. By measuring the water supply with a water supply meter, it is possible to measure the water supply with high accuracy.
【図1】本発明の実施例の説明図。FIG. 1 is an explanatory diagram of an embodiment of the present invention.
【図2】プレート型熱交換器の説明図。FIG. 2 is an explanatory diagram of a plate heat exchanger.
【図3】従来の廃湯熱回収システムの説明図。FIG. 3 is an explanatory view of a conventional waste water heat recovery system.
【図4】従来の木枠構成の廃湯熱回収器の説明図。FIG. 4 is an explanatory view of a waste water heat recovery device having a conventional wooden frame structure.
1 給水槽 2 熱源機 3 給水ライン 4 洗い場 5、5a 廃湯ライン 6 廃湯熱回収器 9 貯湯槽 10 貯湯水位センサ 11 廃湯槽 12 廃湯ポンプ 13 水位センサ 14 流量制御バルブ 15 制御器 1 Water Supply Tank 2 Heat Source Machine 3 Water Supply Line 4 Washing Station 5, 5a Waste Hot Water Line 6 Waste Hot Water Heat Recovery Device 9 Hot Water Storage Tank 10 Hot Water Storage Level Sensor 11 Waste Hot Water Tank 12 Waste Hot Water Pump 13 Water Level Sensor 14 Flow Control Valve 15 Controller
Claims (3)
機に至る給水ラインに流量制御バルブを取り付けたこ
と、 前記熱源機で加熱された温水を貯湯する貯湯槽内に複数
の水位を検出するための貯湯水位センサを取り付けたこ
と、 廃湯を一旦廃湯槽内に溜めてから廃湯ポンプを利用して
汲み揚げ、これを前記廃湯熱回収器を経由して排水する
ように構成したこと、 前記貯湯水位センサで検出される水位に合わせて前記流
量制御バルブを制御し、且つこの流量制御バルブで制御
される水量の70〜100%の廃湯を廃湯槽内から汲み
揚げて廃湯熱回収器内に送り込むように、前記廃湯ポン
プを制御する制御器を設けたこと、 を特徴とする廃湯熱回収システム。1. A flow control valve is attached to a water supply line from a water storage tank to a heat source device via a waste water heat recovery device, and a plurality of water levels are stored in the hot water tank for storing hot water heated by the heat source device. A hot-water storage water level sensor was installed to detect that the waste water was once stored in the waste-water tank and was then pumped up using the waste-water pump, which was then drained via the waste-water heat collector. The flow control valve is controlled according to the water level detected by the hot water storage water level sensor, and 70 to 100% of the amount of water controlled by the flow control valve is pumped up from the waste water tank. A waste water heat recovery system, characterized in that a controller for controlling the waste water pump is provided so as to be fed into the waste water heat recovery device.
サを取り付けて廃湯槽内の水位を検出し、この水位が規
定以下に下った場合には廃湯ポンプでの汲み揚げを停止
し、規定水位以上に上昇した場合には貯湯槽内の水位と
は関係なく汲み揚げを行ってオーバーフローしないよう
に制御する安全回路を設けて成る廃湯熱回収システム。2. The method according to claim 1, wherein a water level sensor is installed in the waste water tank to detect the water level in the waste water tank, and when the water level falls below a prescribed level, pumping by the waste water pump is stopped, A waste hot water heat recovery system that is equipped with a safety circuit that controls pumping to prevent overflow when the water level rises above the specified level regardless of the water level in the hot water storage tank.
としてプレート式熱交換器を用いて成る廃湯熱回収シス
テム。3. The waste hot water heat recovery system according to claim 1, wherein a plate heat exchanger is used as the waste hot water heat recoverer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26773594A JPH08128726A (en) | 1994-10-31 | 1994-10-31 | Waste water heat recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26773594A JPH08128726A (en) | 1994-10-31 | 1994-10-31 | Waste water heat recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08128726A true JPH08128726A (en) | 1996-05-21 |
Family
ID=17448852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26773594A Pending JPH08128726A (en) | 1994-10-31 | 1994-10-31 | Waste water heat recovery system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08128726A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113803883A (en) * | 2013-06-18 | 2021-12-17 | 苏纳珀有限公司 | energy storage system |
-
1994
- 1994-10-31 JP JP26773594A patent/JPH08128726A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113803883A (en) * | 2013-06-18 | 2021-12-17 | 苏纳珀有限公司 | energy storage system |
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