JPS618196A - Apparatus for intermittently supplying ozone - Google Patents
Apparatus for intermittently supplying ozoneInfo
- Publication number
- JPS618196A JPS618196A JP12974684A JP12974684A JPS618196A JP S618196 A JPS618196 A JP S618196A JP 12974684 A JP12974684 A JP 12974684A JP 12974684 A JP12974684 A JP 12974684A JP S618196 A JPS618196 A JP S618196A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- ejector
- valve
- adsorption
- desorption tower
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
Description
【発明の詳細な説明】 〔発明の技術分野〕 本発明は間欠オゾン供給装置に関するものである。[Detailed description of the invention] [Technical field of invention] The present invention relates to an intermittent ozone supply device.
発電所や化学工業等には多量の冷却水が使用されている
が、用水中の微生物や藻類によってスライム障害が発生
し、管路の閉塞や熱褒換率の低下が起こる。これらの防
止策として、高濃度のオゾン水の適用が考慮されている
。この高濃度のオゾン水を生成するためには、大容量の
オゾン発生機を用いて生成するよりも、小形で小容量の
オゾン発生機を用いて、生成したオゾンを吸着剤に長期
いわゆる間欠オゾン供給装置が設備費および運転費用の
点から有利である。Large amounts of cooling water are used in power plants, chemical industries, etc., but microorganisms and algae in the water cause slime problems, clogging pipes and reducing heat exchange rates. As a preventive measure against these problems, the application of highly concentrated ozonated water is being considered. In order to generate this highly concentrated ozone water, rather than using a large-capacity ozone generator, it is necessary to use a small, small-capacity ozone generator and use the generated ozone as an adsorbent to produce long-term so-called intermittent ozone water. The feeding device is advantageous in terms of equipment and operating costs.
従来の代表的な間欠オゾン供給装置の一例を第1図につ
いて説明する。第1図は従来の間欠オゾン供給装置を示
すフロー図であり、図において、(1)はオゾン発生機
、(2)はこのオゾン発生機で発生したオゾンを吸着し
て蓄積するオゾン吸脱着塔、(3)はこのオゾン吸脱着
塔から酸素ガスをオゾン発生機(1)に循環する循環ブ
ロア、(4)はオゾン発生機(1)に酸素を供給する酸
素供給装置、(5a)。An example of a typical conventional intermittent ozone supply device will be explained with reference to FIG. Figure 1 is a flow diagram showing a conventional intermittent ozone supply device. In the diagram, (1) is an ozone generator, and (2) is an ozone adsorption/desorption tower that adsorbs and accumulates ozone generated by this ozone generator. , (3) is a circulation blower that circulates oxygen gas from the ozone adsorption/desorption tower to the ozone generator (1), (4) is an oxygen supply device that supplies oxygen to the ozone generator (1), and (5a).
(5b)はリサイクル弁、(5C)はエゼクタ弁、(6
)はオゾン吸脱着塔(2)加熱用の熱媒体槽、(7)は
この熱媒体槽に設けられた電気ヒータ、(8)は熱媒体
槽(6)から、オゾン吸脱着塔(2)に熱媒体を供給す
る熱1媒体ポンプ、(9)はオゾン吸脱着塔(2)冷却
用の冷凍機、(10)はオゾン吸脱着塔(2)からオゾ
ンを吸引する水流エゼクタ、 (11)はこのエゼクタ
に被処理水を供給するエゼクタポンプ、(12)は逆止
弁であり、オゾン吸脱着塔(2)からエゼクタ(10)
に至る流路にエゼクタ弁(5C)および逆止弁(12)
が設けられている。(5b) is a recycle valve, (5C) is an ejector valve, (6
) is a heating medium tank for heating the ozone adsorption/desorption tower (2), (7) is an electric heater installed in this heating medium tank, and (8) is a heating medium tank for heating the ozone adsorption/desorption tower (2). (9) is a refrigerator for cooling the ozone adsorption/desorption tower (2); (10) is a water ejector that sucks ozone from the ozone adsorption/desorption tower (2); (11) is an ejector pump that supplies water to be treated to this ejector, and (12) is a check valve that connects the ozone adsorption/desorption tower (2) to the ejector (10).
Ejector valve (5C) and check valve (12) in the flow path leading to
is provided.
オゾン吸脱着塔(2)は二重筒になっており、そのうち
内筒にはオゾン吸着剤が充填され、内筒と外筒の間には
ジャケットが形成されて、熱媒体が昇温時に充填され、
熱媒体槽(6)に連絡している。The ozone adsorption/desorption tower (2) has a double cylinder structure, of which the inner cylinder is filled with ozone adsorbent, and a jacket is formed between the inner cylinder and the outer cylinder, and the heating medium is filled when the temperature rises. is,
It is connected to the heat medium tank (6).
また内筒には蒸発管が巻かれ、冷凍機(9)に連絡して
いる。オゾン吸着剤は一般にシリカゲルが用いられ、熱
媒体としてはエチレングリコール、アルコール類等が使
用されている。Further, an evaporation tube is wound around the inner cylinder and is connected to a refrigerator (9). Silica gel is generally used as the ozone adsorbent, and ethylene glycol, alcohols, etc. are used as the heat medium.
なお上記リサイクル弁(5a)、循環ブロア(3)、オ
ゾン発生機(1)、リサイクル弁(5b)、オゾン吸脱
着塔(2)の順に1つの循環系を構成している。The recycle valve (5a), circulation blower (3), ozone generator (1), recycle valve (5b), and ozone adsorption/desorption tower (2) constitute one circulation system in this order.
次に動作について説明する。この動作にはオゾンの吸着
動作および脱着動作の2動作が主としである。Next, the operation will be explained. This operation mainly includes two operations: an ozone adsorption operation and an ozone desorption operation.
初めに吸着動作について説明する。酸素供給装置(4)
より循環系内に常時一定の圧力で酸素を供給する。リサ
イクル弁(5a) 、 (5b)は開き、エゼクタ弁(
5c)は閉じている。循環ブロア(3)により循環系内
に酸素を流通させると、オゾン発生機(1)の放電空隙
中を通過する間に無声放電により酸素の一部がオゾンに
変換されて、オゾン化酸素となる。このオゾン化酸素は
オゾン吸脱着塔(2)へ搬送される。オゾン吸脱着塔(
2)内のオゾン吸着剤は、オゾンを選択的に吸着し、残
りの酸素は、リサイクル弁(5a)を通り循環ブロア(
3)によりオゾン発生機(1)に返送される。オゾンと
して消費された酸素は、酸素供給装置(4)より適宜補
充される。このときオゾン吸着剤の温度は冷凍機(9)
により−30℃以下に冷却されている。冷凍機(9)は
圧−縮機により熱媒体のフhンまたはアンモニアガスを
高温・高圧に圧縮し、凝縮機で水または空気により熱交
換し冷却された熱媒体は膨張弁で膨張し、オゾン吸脱着
塔(2)内で蒸発して吸着剤を冷]却する。上記オゾン
吸着剤のオゾン吸着量は温度により大きく変化する。例
えば温度を低くするとオゾンの吸着量は増加し、逆に温
度が上昇するとオゾンの吸着量は減少する。したがって
オゾンを脱着する時はオゾン吸着剤の温度を上昇させる
。First, the suction operation will be explained. Oxygen supply device (4)
Oxygen is constantly supplied into the circulatory system at a constant pressure. The recycle valves (5a) and (5b) open and the ejector valve (
5c) is closed. When oxygen is circulated in the circulation system by the circulation blower (3), a part of the oxygen is converted into ozone by silent discharge while passing through the discharge gap of the ozone generator (1), and becomes ozonized oxygen. . This ozonized oxygen is transported to the ozone adsorption/desorption tower (2). Ozone adsorption/desorption tower (
The ozone adsorbent in 2) selectively adsorbs ozone, and the remaining oxygen passes through the recycle valve (5a) and is sent to the circulation blower (
3) is returned to the ozone generator (1). Oxygen consumed as ozone is replenished as appropriate from the oxygen supply device (4). At this time, the temperature of the ozone adsorbent is
It is cooled down to -30°C or lower. The refrigerator (9) uses a compressor to compress a heat medium such as air or ammonia gas to high temperature and high pressure, exchanges heat with water or air in a condenser, and the cooled heat medium is expanded by an expansion valve. The adsorbent is cooled by evaporation in the ozone adsorption/desorption tower (2). The amount of ozone adsorbed by the ozone adsorbent varies greatly depending on the temperature. For example, when the temperature is lowered, the amount of ozone adsorbed increases, and conversely, when the temperature is raised, the amount of ozone adsorbed is decreased. Therefore, when desorbing ozone, the temperature of the ozone adsorbent is increased.
オゾン吸脱着塔(2)のオゾン吸着剤がオゾン飽和吸着
量近くまで吸着すると脱着動作へ移行する。When the ozone adsorbent in the ozone adsorption/desorption tower (2) adsorbs ozone close to the saturated amount of adsorption, it shifts to the desorption operation.
脱着動作ではオゾン発生機(1)、循環ブロア(3)、
冷凍機(9)が稼動を停止し、リサイクル弁(5a)。During the desorption operation, an ozone generator (1), a circulation blower (3),
Refrigerator (9) stops operating and recycle valve (5a).
(5b)が閉じ、熱媒体ポンプ(8)が稼動して吸脱着
基(2)内の昇温を開始する。熱媒体槽(6)内は電気
ヒータ(7)により常に一定の温度になるようにコント
ロールされている。この状態を予備加熱という。(5b) is closed and the heat medium pump (8) is operated to start increasing the temperature inside the adsorption/desorption group (2). The inside of the heat medium tank (6) is controlled to always have a constant temperature by an electric heater (7). This state is called preheating.
吸脱着基(2)内の温度がある一定値になると、エゼク
タポンプ(11)が起動すると同時に、水流エゼクタ(
10)が吸い込み動作を開始し、エゼクタ弁(5c)が
開き吸脱着基(2)内のオゾンを減圧、吸引しながら水
流エゼクタ(10)で水とオゾンとを混合してオゾン水
として使用箇所へ送給する。かくして、吸脱着基(2)
内のオゾンが残り少なくなると脱着期間が終了し、再び
初期の吸着動作へと移行して連続的に運転が繰り返され
る。When the temperature inside the adsorption/desorption group (2) reaches a certain value, the ejector pump (11) starts and at the same time the water ejector (
10) starts the suction operation, and the ejector valve (5c) opens to reduce the pressure and suck the ozone in the adsorption/desorption group (2), while mixing water and ozone in the water jet ejector (10) to be used as ozone water. send to. Thus, the adsorption/desorption group (2)
When there is little ozone left in the tank, the desorption period ends, and the operation returns to the initial adsorption operation, where operation is repeated continuously.
従来の間欠オゾン供給装置は上記のように構成されてい
るので、オゾン処理水管内の圧力が高く、かつエゼクタ
ポンプ(11)が稼動すると同時にエゼクタ弁(10)
が開くため、逆止弁(12)が何が異物により誤動作す
ると、オゾン吸脱着塔(2)内に処理水が逆流し、吸脱
着基(2)内の充填剤を劣化させる危険性があった。Since the conventional intermittent ozone supply device is configured as described above, the pressure inside the ozonated water pipe is high, and the ejector valve (10) is activated at the same time as the ejector pump (11) is activated.
If the check valve (12) malfunctions due to foreign matter, the treated water will flow back into the ozone adsorption/desorption tower (2) and there is a risk of deteriorating the filler in the adsorption/desorption group (2). Ta.
この発明は、上記のような従来のものの欠点を除去する
目的でなされたもので、原料酸素からオゾン化酸素を生
成するオゾン発生機と、上記オゾン化酸素からオゾンを
吸着蓄積し、このオゾンを脱着するオゾン吸脱着塔とを
有し、上記オゾン吸脱着塔によりオゾンが吸着された後
の酸素をオゾン発生機に戻し、かつ上記オゾン吸脱着塔
からオゾンをエゼクタにて脱着供給し、オゾン吸脱着塔
をオゾンの吸着時に冷凍機により冷却するとともに、脱
着時に加熱源により昇温する間欠オゾン供給装置におい
て、オゾン吸脱着塔からエゼクタに至る流路に設けられ
たエゼクタ弁と逆止弁の間に負圧を検知してエゼクタ弁
を開く圧力スイッチを設けることにより、エゼクタのガ
ス吸込み側が負圧になるのを確認してからエゼクタ弁を
開いて、オゾン吸脱着塔への水の逆流を防止でき、信頼
性の高い間欠オゾン供給装置を提供するものである。This invention was made for the purpose of eliminating the drawbacks of the conventional ones as described above, and includes an ozone generator that generates ozonized oxygen from raw material oxygen, and an ozone generator that adsorbs and accumulates ozone from the ozonized oxygen. The ozone adsorption/desorption tower has an ozone adsorption/desorption tower, returns oxygen after ozone has been adsorbed by the ozone adsorption/desorption tower to the ozone generator, and desorbs and supplies ozone from the ozone adsorption/desorption tower with an ejector. In an intermittent ozone supply system in which the desorption tower is cooled by a refrigerator during ozone adsorption and heated by a heating source during ozone desorption, the ozone is removed between the ejector valve and the check valve provided in the flow path from the ozone adsorption/desorption tower to the ejector. By installing a pressure switch that detects negative pressure and opens the ejector valve, the ejector valve opens after confirming that the gas suction side of the ejector has negative pressure, thereby preventing water from flowing back into the ozone adsorption/desorption tower. The present invention provides a highly reliable intermittent ozone supply device.
以下、本発明の実施例を図について説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第2図は本発明の一実施例を示すフロー図であり、図に
おいて、第1図と同一部分には同じ符号を付して説明を
省略する。吸脱着基(2)からエゼクタ(10)に至る
流路に設けられたエゼクタ弁(5c)と逆止弁(12)
との間には、負圧を検知してエゼクタ弁(5c)を開く
圧力スイッチ(13)が設けられている。FIG. 2 is a flow diagram showing an embodiment of the present invention. In the figure, the same parts as those in FIG. Ejector valve (5c) and check valve (12) provided in the flow path from the adsorption/desorption group (2) to the ejector (10)
A pressure switch (13) that detects negative pressure and opens the ejector valve (5c) is provided between the two.
他の構成は第1図と同様である。The other configurations are the same as in FIG. 1.
次に動作について説明する。基本的な動作は第1図の場
合と同様である。Next, the operation will be explained. The basic operation is the same as that shown in FIG.
オゾン吸脱着塔(2)内にはシリカゲル吸着剤が充填さ
れているが、この吸着剤により酸素とオゾンに有効に分
離するためには、シリカゲルに対する水分等の吸着を極
力避けなければその効果は半減する。特に水が逆流して
シリカゲルが水にぬれると、シリカゲルは破損し、使用
不能となる。またシリカゲルは量的にも多いため費用が
かかり、吸脱着基(2)内は充填剤の昇温あるいは冷却
のために複雑な構造になっており、シリカゲルの取り出
しおよび充填に相当の時間を必要とするので、シリカゲ
ル充填内への水の浸入を防ぐ必要がある。The ozone adsorption/desorption tower (2) is filled with a silica gel adsorbent, but in order for this adsorbent to effectively separate oxygen and ozone, the adsorption of water, etc. to the silica gel must be avoided as much as possible. Reduce by half. In particular, if water flows backward and the silica gel gets wet, the silica gel will be damaged and become unusable. In addition, silica gel is expensive because it is large in quantity, and the adsorption/desorption group (2) has a complicated structure for heating or cooling the filler, so it takes a considerable amount of time to remove and fill the silica gel. Therefore, it is necessary to prevent water from entering the silica gel filling.
第2図において、エゼクタ弁(5c)と逆止弁(12)
との間に取り付けられた圧力スイッチ(13)はエゼク
タ弁(5c)の開放動作に対し、必要条件として機能す
る。この場合、エゼクタポンプ(11)が起動し、エゼ
クタ弁(5c)とエゼクタ(10)の間の配管が負圧に
なって初めて圧力スイッチ(13)が負圧を検知し、こ
れによりエゼクタ弁(5c)が開く。この条件を満して
おれば、吸脱着基(2)内の圧力は必ず上記配管と同圧
または高圧になり、オゾン吸脱着塔(2)に水が逆流す
ることはない。例えば、逆止弁(12)に□何か異物が
入り完全に閉じない場合は、水がエゼクタ弁(5c)の
出口まで到達するが、圧力スイッチ(13)は負圧を検
知しないのでエゼクタ弁(5c)は開くことはない。ま
た圧力スイッチ(13)を2位置設定にすれば、外部に
異常警報を出すことができる。In Figure 2, the ejector valve (5c) and check valve (12)
The pressure switch (13) installed between the ejector valve (5c) serves as a prerequisite for the opening operation of the ejector valve (5c). In this case, the pressure switch (13) detects negative pressure only after the ejector pump (11) is started and the piping between the ejector valve (5c) and the ejector (10) becomes negative pressure, which causes the ejector valve ( 5c) opens. If this condition is met, the pressure inside the adsorption/desorption group (2) will always be the same or higher than the pressure in the piping, and water will not flow back into the ozone adsorption/desorption tower (2). For example, if some foreign object enters the check valve (12) and it does not close completely, water will reach the outlet of the ejector valve (5c), but the pressure switch (13) will not detect negative pressure, so the ejector valve (5c) will never open. Moreover, if the pressure switch (13) is set to 2 positions, an abnormality alarm can be issued to the outside.
第3図は他の実施例を示すフロー図であり、図において
、吸脱着基(2)からエゼクタ(10)に至る流路に設
けられたエゼクタ弁(5C)と逆止弁(12)との間に
、上流側より、負圧を検知してエゼクタ弁(5c)を開
く圧力スイッチ(13)、およびエゼクタポンプ(11
)の駆動とともに開放する締切弁(14)とがこの順序
で設けられている。他の構成は第1図と同様である。FIG. 3 is a flow diagram showing another embodiment, and in the figure, an ejector valve (5C) and a check valve (12) provided in the flow path from the adsorption/desorption group (2) to the ejector (10) are shown. Meanwhile, from the upstream side, a pressure switch (13) that detects negative pressure and opens the ejector valve (5c) and an ejector pump (11) are activated.
) are provided in this order. The other configurations are the same as in FIG. 1.
次に動作について説明する。エゼクタ弁(5C)と締切
弁(14)との間に取り付けられた圧力スイッチ(13
)はエゼクタ弁(5c)の開放動作の必要条件として機
能する。ここではエゼクタポンプ(11)が起動し、締
切弁(14)が開き、エゼクタ弁(5C)とエゼクタ(
10)の間の配管が負圧になって初めて圧力スイッチ(
13)が負圧を検知し、エゼクタ弁(5c)が開く。Next, the operation will be explained. The pressure switch (13) installed between the ejector valve (5C) and the shutoff valve (14)
) serves as a necessary condition for the opening operation of the ejector valve (5c). Here, the ejector pump (11) starts, the shutoff valve (14) opens, and the ejector valve (5C) and ejector (
10) The pressure switch (
13) detects negative pressure and the ejector valve (5c) opens.
締切弁(14)は圧力スイッチ(13)と逆止弁(12
)の間に取り付けられており、エゼクタポンプ(11)
の駆動と同時に開放になる。締切弁(14)がないと、
逆止弁(12)に異物が入った場合、水が逆流し圧力ス
イッチ(13)により装置が停止するが、被処理水内に
SS、スライム等が多いときはこの異常が出ることが多
い。これに対し、締切弁(14)を圧力スイッチ(13
)と逆止弁(12)の間に設けると、逆止弁(12)に
よる異常表示現象を少なくするとともに、水の逆流防止
に対しては、締切弁(14)がないときに較べて相当信
頼性が高くなる。異常が出た場合は本装置としては厳重
大事故につながるが、上記によりこのようなことが防止
される。また異常が発生した場合には、エゼクタ弁(5
C)および締切弁(14)は同時に閉じる。The shutoff valve (14) has a pressure switch (13) and a check valve (12).
) and is installed between the ejector pump (11)
It becomes open at the same time as driving. Without the shutoff valve (14),
If foreign matter enters the check valve (12), water will flow back and the pressure switch (13) will shut down the device, but this abnormality often occurs when there are a lot of SS, slime, etc. in the water to be treated. On the other hand, the shutoff valve (14) is connected to the pressure switch (13).
) and the check valve (12), it will reduce the abnormal display phenomenon caused by the check valve (12), and will be more effective in preventing backflow of water than when there is no shutoff valve (14). Increased reliability. If an abnormality were to occur, this would lead to a serious accident, but the above prevents this from happening. In addition, if an abnormality occurs, the ejector valve (5
C) and the shut-off valve (14) are closed simultaneously.
なお、上記の説明において、エゼクタ弁(5C)として
はノンリークであれば電磁弁、エテーシリンダ弁、電動
弁のいずれでもよいが、このうち電動弁はその開閉の速
度に充分注意する必要がある。In the above description, the ejector valve (5C) may be a solenoid valve, an electric cylinder valve, or an electric valve as long as it is non-leak, but it is necessary to pay sufficient attention to the opening and closing speed of the electric valve.
ままた、上記説明においては、圧力スイッチ(13)と
して2位置設定のものを示したが、圧力スイッチを2個
取り付けてもよい。さらに本発明は冷却水に限らず、他
の液体等にオゾンを供給する場合にも適用可能である。Furthermore, in the above description, the pressure switch (13) is shown as having two positions, but two pressure switches may be installed. Furthermore, the present invention is applicable not only to cooling water but also to cases where ozone is supplied to other liquids.
以上のとおり、この発明によれば、エゼクタ弁と逆止弁
の間に圧力スイッチを設けたので、圧力スイッチで負圧
になったことを検出した後エゼクタ弁が開くため、水の
逆流は起こらず、逆止弁に異物が混入して動作不良を起
こした場合でも、水の逆流の危険が全くないという効果
が得られる。As described above, according to the present invention, since the pressure switch is provided between the ejector valve and the check valve, the ejector valve opens after the pressure switch detects that the pressure has become negative, so that no backflow of water occurs. First, even if foreign matter gets into the check valve and causes malfunction, there is no risk of water backflow.
また、エゼクタ弁と逆止弁の間に圧力スイッチおよび締
切弁を設ければ、逆止弁の誤動作による異常発生が少な
くなるとともに、吸脱着基への水の逆流防止の信頼性が
さらに高まり、安定性の高い装置が得られる効果がある
。In addition, if a pressure switch and a shutoff valve are installed between the ejector valve and the check valve, the occurrence of abnormalities due to malfunction of the check valve will be reduced, and the reliability of preventing the backflow of water to the adsorption/desorption group will be further increased. This has the effect of providing a highly stable device.
第1図は従来の間欠オゾン供給装置を示すフロー図、第
2、図および第3図はこの発明の別の実施例1こよる間
欠オゾン供給装置を示すフロー図である。
図において、(1)はオゾン発生機、(2)はオゾン吸
脱着塔、(3)はf!環ブロア、(4)は酸素供給装置
、(5a) 、 (5b)はリサイクル弁、(5C)は
エゼクタ弁、(6)は熱媒体槽、(7)は電気ヒータ、
(8)は熱媒体ポンプ、(9)は冷凍機、(10)はエ
ゼクタ、(11)はなお、各図中、同一符号は同一また
は相当部分を示す。FIG. 1 is a flowchart showing a conventional intermittent ozone supply device, and FIGS. 2, 2, and 3 are flowcharts showing an intermittent ozone supply device according to another embodiment 1 of the present invention. In the figure, (1) is an ozone generator, (2) is an ozone adsorption/desorption tower, and (3) is f! Ring blower, (4) is oxygen supply device, (5a), (5b) are recycle valves, (5C) is ejector valve, (6) is heat medium tank, (7) is electric heater,
(8) is a heat medium pump, (9) is a refrigerator, (10) is an ejector, and (11) is a heat transfer medium pump. In each figure, the same reference numerals indicate the same or corresponding parts.
Claims (4)
機と、上記オゾン化酸素からオゾンを吸着蓄積し、この
オゾンを脱着するオゾン吸脱着塔とを有し、上記オゾン
吸脱着塔によりオゾンが吸着された後の酸素をオゾン発
生機に戻し、かつ上記オゾン吸脱着塔からオゾンをエゼ
クタにて脱着供給し、オゾン吸脱着塔をオゾンの吸着時
に冷凍機により冷却するとともに、脱着時に加熱源によ
り昇温する間欠オゾン供給装置において、オゾン吸脱着
塔からエゼクタに至る流路に設けられたエゼクタ弁と逆
止弁との間に、負圧を検知してエゼクタ弁を開く圧力ス
イッチを設けたことを特徴とする間欠オゾン供給装置。(1) It has an ozone generator that generates ozonized oxygen from raw material oxygen, and an ozone adsorption/desorption tower that adsorbs and accumulates ozone from the ozonized oxygen and desorbs this ozone, and the ozone adsorption/desorption tower generates ozone. The adsorbed oxygen is returned to the ozone generator, and ozone is desorbed and supplied from the ozone adsorption/desorption tower using an ejector, and the ozone adsorption/desorption tower is cooled by a refrigerator during ozone adsorption, and is cooled by a heating source during desorption. In an intermittent ozone supply device that increases temperature, a pressure switch is installed between an ejector valve and a check valve provided in a flow path from an ozone adsorption/desorption tower to an ejector to detect negative pressure and open the ejector valve. An intermittent ozone supply device featuring:
いることを特徴とする特許請求の範囲第1項記載の間欠
オゾン供給装置。(2) The intermittent ozone supply device according to claim 1, characterized in that the pressure switch is set at two positions or is provided with two pressure switches.
機と、上記オゾン化酸素からオゾンを吸着蓄積し、この
オゾンを脱着するオゾン吸脱着塔とを有し、上記オゾン
吸脱着塔によりオゾンが吸着された後の酸素をオゾン発
生機に戻し、かつ上記オゾン吸脱着塔からオゾンをエゼ
クタにて脱着供給し、オゾン吸脱着塔をオゾンの吸着時
に冷凍機により冷却するとともに、脱着時に加熱源によ
り昇温する間欠オゾン供給装置において、オゾン吸脱着
塔からエゼクタに至る流路に設けられたエゼクタ弁と逆
止弁との間に、上流側より、負圧を検知してエゼクタ弁
を開く圧力スイッチ、およびエゼクタポンプの駆動とと
もに開放する締切弁を設けたことを特徴とする間欠オゾ
ン供給装置。(3) It has an ozone generator that generates ozonized oxygen from raw material oxygen, and an ozone adsorption/desorption tower that adsorbs and accumulates ozone from the ozonized oxygen and desorbs the ozone, and the ozone adsorption/desorption tower generates ozone. The adsorbed oxygen is returned to the ozone generator, and ozone is desorbed and supplied from the ozone adsorption/desorption tower using an ejector, and the ozone adsorption/desorption tower is cooled by a refrigerator during ozone adsorption, and is cooled by a heating source during desorption. In an intermittent ozone supply device that increases temperature, a pressure switch is installed from the upstream side between an ejector valve and a check valve installed in the flow path from the ozone adsorption/desorption tower to the ejector to open the ejector valve by detecting negative pressure. , and an intermittent ozone supply device characterized by being provided with a shutoff valve that opens when the ejector pump is driven.
動弁であることを特徴とする特許請求の範囲第3項記載
の間欠オゾン供給装置。(4) The intermittent ozone supply device according to claim 3, wherein the ejector valve is a solenoid valve, an air cylinder valve, or an electric valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12974684A JPS618196A (en) | 1984-06-23 | 1984-06-23 | Apparatus for intermittently supplying ozone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12974684A JPS618196A (en) | 1984-06-23 | 1984-06-23 | Apparatus for intermittently supplying ozone |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS618196A true JPS618196A (en) | 1986-01-14 |
| JPH022632B2 JPH022632B2 (en) | 1990-01-18 |
Family
ID=15017176
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12974684A Granted JPS618196A (en) | 1984-06-23 | 1984-06-23 | Apparatus for intermittently supplying ozone |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS618196A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63152491A (en) * | 1986-12-10 | 1988-06-24 | 泉製紙有限会社 | Deinking apparatus for pulping treatment of papermaking old paper raw material |
| JPH02198693A (en) * | 1989-01-27 | 1990-08-07 | Apanasu:Kk | Ozone water cleaner |
| US4977943A (en) * | 1988-05-14 | 1990-12-18 | Jujo Paper Co., Ltd. | Waste paper de-inking process using multi-stage vertical column vapor-liquid mixer |
| JP2014517767A (en) * | 2011-05-17 | 2014-07-24 | バイオケル ユーケイ リミテッド | Ozone wound disinfection device and its leak test procedure |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5206547B2 (en) * | 2009-03-30 | 2013-06-12 | 三菱電機株式会社 | Ozone production apparatus and method for producing ozone |
-
1984
- 1984-06-23 JP JP12974684A patent/JPS618196A/en active Granted
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63152491A (en) * | 1986-12-10 | 1988-06-24 | 泉製紙有限会社 | Deinking apparatus for pulping treatment of papermaking old paper raw material |
| US4977943A (en) * | 1988-05-14 | 1990-12-18 | Jujo Paper Co., Ltd. | Waste paper de-inking process using multi-stage vertical column vapor-liquid mixer |
| JPH02198693A (en) * | 1989-01-27 | 1990-08-07 | Apanasu:Kk | Ozone water cleaner |
| JP2014517767A (en) * | 2011-05-17 | 2014-07-24 | バイオケル ユーケイ リミテッド | Ozone wound disinfection device and its leak test procedure |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH022632B2 (en) | 1990-01-18 |
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