JPS6130060Y2 - - Google Patents

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Publication number
JPS6130060Y2
JPS6130060Y2 JP15398182U JP15398182U JPS6130060Y2 JP S6130060 Y2 JPS6130060 Y2 JP S6130060Y2 JP 15398182 U JP15398182 U JP 15398182U JP 15398182 U JP15398182 U JP 15398182U JP S6130060 Y2 JPS6130060 Y2 JP S6130060Y2
Authority
JP
Japan
Prior art keywords
washing water
molten salt
tank
water tank
washing
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
Application number
JP15398182U
Other languages
Japanese (ja)
Other versions
JPS5959674U (en
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 filed Critical
Priority to JP15398182U priority Critical patent/JPS5959674U/en
Publication of JPS5959674U publication Critical patent/JPS5959674U/en
Application granted granted Critical
Publication of JPS6130060Y2 publication Critical patent/JPS6130060Y2/ja
Granted legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は溶融塩を用いて高温固体から熱を回収
する際の装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for recovering heat from a high temperature solid using a molten salt.

溶融塩を用いて高温固体から熱を回収する方法
について従来のものの概用を第1図を用いて説明
する。
A general description of a conventional method for recovering heat from a high-temperature solid using molten salt will be given with reference to FIG.

高温固体1を溶融塩槽3中に浸し、より低温の
溶融塩2に熱伝達した後、引き上げて洗浄水槽5
に送りライン10からの洗浄水で付着した溶融塩
を洗い落とし、冷却された固体6は次工程へ送
る。前記槽3内の溶融塩2中には蒸発管7を設
け、蒸気ドラム9で蒸気は分離し、ライン8から
需要先へ送る。蒸発管7は溶融塩槽3の上部へ設
け、溶融塩2の自然循環を利用するか、あるいは
強制循環装置を設け高温の溶融塩2と蒸発管7が
接するようにする。
The high-temperature solid 1 is immersed in a molten salt tank 3, and after heat is transferred to the lower-temperature molten salt 2, it is pulled out and placed in a washing water tank 5.
The adhering molten salt is washed off with washing water from the feed line 10, and the cooled solid 6 is sent to the next process. An evaporation pipe 7 is provided in the molten salt 2 in the tank 3, and the steam is separated in a steam drum 9 and sent to a consumer through a line 8. The evaporation pipe 7 is provided above the molten salt tank 3, and the molten salt 2 is naturally circulated, or a forced circulation device is provided so that the high temperature molten salt 2 and the evaporation pipe 7 come into contact with each other.

ここで、溶融塩2の回収方法について着目する
と、従来は溶融塩を含む洗浄水11を、ライン4
から少しづつ溶融塩槽3に送り、槽内で水を蒸発
させて溶融塩を回収していた。この方法では洗浄
水11を多量に溶融塩槽3に送りこめないので、
洗浄水槽5中の塩濃度はしだいに高くなつて洗浄
効果が低下する。あるいは、塩濃度がある程度高
くなると、洗浄水槽内の洗浄水をすべてぬき出し
て、他の溶融塩回収装置へ送り、処理して回収を
行つていた。
Here, focusing on the method for recovering the molten salt 2, conventionally the washing water 11 containing the molten salt is collected through the line 4.
The molten salt was sent little by little to the molten salt tank 3, and the water was evaporated in the tank to recover the molten salt. With this method, a large amount of washing water 11 cannot be sent to the molten salt tank 3, so
The salt concentration in the cleaning water tank 5 gradually increases and the cleaning effect decreases. Alternatively, when the salt concentration reaches a certain level, all of the washing water in the washing tank is drained and sent to another molten salt recovery device for treatment and recovery.

本考案は溶融塩を回収する際の上記のような問
題点を解決するために洗浄水槽からぬき出した洗
浄水を真空濃縮装置(あるいは完全乾燥した微小
結晶粒としてとり出す真空晶析装置)へ送り、濃
縮した洗浄水(あるいは析出した塩)を再び溶融
塩槽内へもどし再利用するようにしたもので、高
温固体からの熱回収用溶融塩槽、固体に付着した
溶融塩洗浄用洗浄水槽および洗浄水抜き出し管を
介して洗浄水槽と連結されると共に、濃縮洗浄水
もしくは析出溶融塩抜き出し管を介して溶融塩槽
と連結された真空容器からなる、高温固体からの
熱回収装置に関するものである。
This invention solves the above-mentioned problems when recovering molten salt by transferring the washing water drained from the washing water tank to a vacuum concentrator (or a vacuum crystallizer that extracts it as completely dried microcrystal grains). The concentrated washing water (or precipitated salt) is returned to the molten salt tank and reused.It is used as a molten salt tank for heat recovery from high-temperature solids, and a washing water tank for washing molten salt adhered to solids. and a heat recovery device from high-temperature solids, which comprises a vacuum vessel connected to a washing water tank via a washing water extraction pipe and a molten salt tank via a concentrated washing water or precipitated molten salt extraction pipe. be.

本考案の装置は溶融塩を利用した鋼板の熱処理
装置、鋼板からの熱回収装置、線材からの熱回収
装置に有効に適用できる。
The device of the present invention can be effectively applied to a steel plate heat treatment device using molten salt, a heat recovery device from a steel plate, and a heat recovery device from a wire rod.

第2図、第3図を用いて本考案装置について具
体的に説明する。
The device of the present invention will be specifically explained using FIGS. 2 and 3.

洗浄水槽5の底部に洗浄水ぬき出し管4を設け
る。ポンプ17で、あるいはポンプを用いず洗浄
水槽と真空容器の圧力差で、洗浄水11を真空容
器12へ圧送し、容器内で噴射・霧化させる。洗
浄水を濃縮液として回収する場合は、第2図に示
すように容器内に濃縮効率を高めるための充てん
層13を設け、真空容器の底部にぬき出し管14
を設ける。ぬき出し管14から濃縮洗浄水を連続
的あるいは間欠的に溶融塩槽へ戻す。乾燥した塩
として回収する場合には、第3図に示すように、
洗浄水のぬき出し管4にヒータ19を設け、真空
容器12の底部に、乾燥塩のぬき出し管18を設
ける。真空容器12内のガスはミストセパレータ
15を介して真空ポンプ16でぬき出す。他の構
造は第1図と同様である。
A washing water drain pipe 4 is provided at the bottom of the washing water tank 5. The cleaning water 11 is pumped to the vacuum container 12 by the pump 17 or by the pressure difference between the cleaning water tank and the vacuum container without using a pump, and is sprayed and atomized within the container. When recovering the washing water as a concentrated liquid, as shown in Fig. 2, a filling layer 13 is provided in the container to increase the concentration efficiency, and a drain pipe 14 is provided at the bottom of the vacuum container.
will be established. The concentrated washing water is continuously or intermittently returned to the molten salt tank from the drain pipe 14. When recovering as dry salt, as shown in Figure 3,
A heater 19 is provided in the cleaning water outlet pipe 4, and a dry salt outlet pipe 18 is provided at the bottom of the vacuum container 12. Gas in the vacuum container 12 is extracted by a vacuum pump 16 via a mist separator 15. The other structure is the same as that in FIG.

洗浄水槽5からぬき出した洗浄水11を真空容
器12内へ送りこむことにより、容器内でただち
に洗浄水の真空蒸発が起る。このとき、洗浄水を
容器内でスプレすれば、水の比表面積を増大させ
ることができる為、蒸発量は著しく増大する。容
器内へスプレされた洗浄水は溶媒である水が蒸発
して、第2図に示すように濃縮液あるいは飽和液
として、または第3図に示すように析出結晶粒と
していづれかの状態でとり出すことができる。
By sending the cleaning water 11 drawn out from the cleaning water tank 5 into the vacuum container 12, vacuum evaporation of the cleaning water immediately occurs within the container. At this time, if the cleaning water is sprayed inside the container, the specific surface area of the water can be increased, and therefore the amount of evaporation can be significantly increased. The water as a solvent in the washing water sprayed into the container evaporates and is taken out either as a concentrated liquid or saturated liquid as shown in Figure 2, or as precipitated crystal grains as shown in Figure 3. be able to.

本考案装置を用いることにより次のような効果
が奏せられる。
By using the device of the present invention, the following effects can be achieved.

1 洗浄水槽から洗浄水を連続的にぬき出し、同
量の洗浄水(純水)を補給できる為、洗浄効率
が上昇する。
1. Washing water can be continuously drawn out from the washing water tank and the same amount of washing water (pure water) can be replenished, increasing washing efficiency.

2 真空濃縮装置あるいは真空晶析装置で濃縮あ
るいは晶析した溶融塩をそのまま溶融塩槽にも
どすことにより、直ちに再利用できる。
2. Molten salt concentrated or crystallized in a vacuum concentrator or vacuum crystallizer can be immediately reused by returning it to the molten salt tank.

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

添付の図面は高温固体からの熱回収装置の概要
を示す模式図であり、第1図が従来のもの、第2
図、第3図が本考案のものである。図中3が溶融
塩槽、5が洗浄水槽、12が真空容器、4が洗浄
水抜き出し管、14が濃縮洗浄水抜き出し管、1
8が析出溶融塩抜き出し管である。
The attached drawings are schematic diagrams showing the outline of a heat recovery device from high-temperature solids.
Figure 3 shows the present invention. In the figure, 3 is a molten salt tank, 5 is a washing water tank, 12 is a vacuum container, 4 is a washing water extraction pipe, 14 is a concentrated washing water extraction pipe, 1
8 is a precipitated molten salt extraction pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 高温固体からの熱回収用溶融塩槽、固体に付着
した溶融塩洗浄用洗浄水槽および洗浄水抜き出し
管を介して洗浄水槽と連結されると共に、濃縮洗
浄水もしくは析出溶融塩抜き出し管を介して溶融
塩槽と連結された真空容器からなる、高温固体か
らの熱回収装置。
It is connected to a molten salt tank for heat recovery from high-temperature solids, a washing water tank for washing molten salt attached to solids, and a washing water tank via a washing water extraction pipe, and is also connected to a washing water tank for removing concentrated washing water or precipitated molten salt via a extraction pipe. A device for recovering heat from high temperature solids, consisting of a vacuum vessel connected to a salt bath.
JP15398182U 1982-10-13 1982-10-13 Heat recovery device from high temperature solids Granted JPS5959674U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15398182U JPS5959674U (en) 1982-10-13 1982-10-13 Heat recovery device from high temperature solids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15398182U JPS5959674U (en) 1982-10-13 1982-10-13 Heat recovery device from high temperature solids

Publications (2)

Publication Number Publication Date
JPS5959674U JPS5959674U (en) 1984-04-18
JPS6130060Y2 true JPS6130060Y2 (en) 1986-09-03

Family

ID=30340506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15398182U Granted JPS5959674U (en) 1982-10-13 1982-10-13 Heat recovery device from high temperature solids

Country Status (1)

Country Link
JP (1) JPS5959674U (en)

Also Published As

Publication number Publication date
JPS5959674U (en) 1984-04-18

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