JPH0942501A - Safety valve for treating vessel - Google Patents
Safety valve for treating vesselInfo
- Publication number
- JPH0942501A JPH0942501A JP20833495A JP20833495A JPH0942501A JP H0942501 A JPH0942501 A JP H0942501A JP 20833495 A JP20833495 A JP 20833495A JP 20833495 A JP20833495 A JP 20833495A JP H0942501 A JPH0942501 A JP H0942501A
- Authority
- JP
- Japan
- Prior art keywords
- safety valve
- processing tank
- fluid
- pipe line
- depressurizing
- 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
- 239000012530 fluid Substances 0.000 claims abstract description 24
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 40
- 239000007788 liquid Substances 0.000 claims description 33
- 238000012545 processing Methods 0.000 claims description 22
- 238000011049 filling Methods 0.000 claims description 10
- 239000011521 glass Substances 0.000 claims description 10
- 238000007670 refining Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 description 9
- 230000008020 evaporation Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 238000011084 recovery Methods 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Safety Valves (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、例えば使用済みの硫
酸を再生する硫酸回収装置の蒸留塔や蒸発塔において、
圧力上昇による装置の破損を防止するための処理槽の安
全弁に関する。BACKGROUND OF THE INVENTION The present invention relates to, for example, a distillation column or an evaporation column of a sulfuric acid recovery device for regenerating used sulfuric acid,
The present invention relates to a safety valve for a processing tank for preventing damage to the device due to an increase in pressure.
【0002】[0002]
【従来の技術】図5は、使用済みの硫酸を濃縮し、精製
して再生させる硫酸回収装置を示すもので、水分を蒸発
させて除去する濃縮塔1と、硫酸蒸気を蒸発させて不純
物と分離する蒸発塔2と、蒸発した気体を液化して回収
する凝縮器3,4、及びその他の付帯設備から構成さ
れ、これらの装置の大部分は耐食性を確保するためにガ
ラスから製造されている。2. Description of the Related Art FIG. 5 shows a sulfuric acid recovery apparatus for concentrating, refining and regenerating used sulfuric acid. The concentrating tower 1 evaporates and removes water, and the sulfuric acid vapor evaporates to remove impurities. It consists of an evaporation tower 2 for separation, condensers 3 and 4 for liquefying and recovering the evaporated gas, and other incidental equipment, and most of these devices are made of glass to ensure corrosion resistance. .
【0003】濃縮塔1及び蒸発塔2は、下側が貯留部
5,6とされ、ヒータ7,8によって所定の温度(濃縮
塔:310〜320℃、蒸発塔:約330℃)に維持さ
れている。中段部には、小片状のラシヒリング9が充填
されて形成された充填層11,12が、上部には内部に
冷却オイルが流通する冷却器13,14が設けられてい
る。頂部には、蒸気を排出する排出管15,16が設け
られ、これには凝縮器3,4が取り付けられ、凝縮器3
はドレンに、凝縮器4は精製硫酸の回収容器に通じてい
る。The lower sides of the concentrating tower 1 and the evaporating tower 2 are storage parts 5 and 6, and are maintained at predetermined temperatures (concentrating tower: 310 to 320 ° C., evaporating tower: about 330 ° C.) by heaters 7 and 8. There is. Filled layers 11 and 12 formed by filling a small piece of Raschig ring 9 are provided in the middle part, and coolers 13 and 14 through which cooling oil flows are provided in the upper part. Discharge pipes 15 and 16 for discharging steam are provided at the top, and condensers 3 and 4 are attached to the discharge pipes 15 and 16, respectively.
Is connected to a drain, and the condenser 4 is connected to a purified sulfuric acid recovery container.
【0004】濃縮塔1の充填層11の上側には廃硫酸の
供給口17が設けられ、貯留部5には、濃縮した液体を
次工程の蒸発塔2に送る送液管18が設けられている。
図4の(a)に示すように、ラヒシリング9はガラス製
の径10mm、長さ10mm程度の管状の小片で、これが支
持構造によって支えられて網状空間を擁する充填層1
1,12を構成している。なお、この充填物としては、
同図(b),(c)に示すように中に仕切のあるレッシ
ングリング9a、複数のリングが複合した形状の小片9
b、鞍型の小片等、空隙が大きく、流下液が均一に流下
し、表面積が大きくて軽いものが用いられる。材質は、
陶磁器、金属、プラスチック等から処理対象の流体に適
合したものが用いられるが、硫酸の場合はガラスであ
る。A supply port 17 for waste sulfuric acid is provided above the packed bed 11 of the concentration tower 1, and a liquid feed pipe 18 for feeding the concentrated liquid to the evaporation tower 2 of the next step is provided in the storage part 5. There is.
As shown in FIG. 4 (a), the lahi ring 9 is a glass-made tubular piece having a diameter of 10 mm and a length of 10 mm, which is supported by a supporting structure and has a reticulated space 1
1 and 12 are configured. In addition, as this filling,
As shown in (b) and (c) of the figure, a lessing ring 9a having a partition therein, and a small piece 9 having a shape in which a plurality of rings are combined
b, a saddle-shaped small piece, or the like, which has large voids, allows the downflowing liquid to uniformly flow down, and has a large surface area and is light. The material is
A material suitable for the fluid to be treated is used from ceramics, metals, plastics, etc., but in the case of sulfuric acid, it is glass.
【0005】濃縮塔1の貯留部5では、加熱によって濃
度約70%の硫酸が蒸発し、充填層11中を上昇する。
一方、供給口17からは廃硫酸液が供給され、充填層中
を下降する。充填層11では、このように気相と液相が
対向する流れを形成し、上方へ向かうに従い低下する温
度勾配が形成されている。そして、対向して流れる気相
と液相の間で熱交換と物質の移動が行われ、結果として
硫酸濃度の低い蒸気が充填層11上面から上昇し、硫酸
濃度の高い液体がラシヒリング9を伝って貯留部5に環
流する。上昇する蒸気は冷却器13で冷却されてその一
部が凝縮して充填層11に流れ、残りは排出管15から
凝縮器3へ流れて液化し、5%程度の希硫酸としてドレ
ンへ排出される。蒸発塔2では、濃度約96%の硫酸が
蒸発し、充填層12、冷却器14を経て凝縮器4に至
り、製品として回収される。In the storage section 5 of the concentrating tower 1, sulfuric acid having a concentration of about 70% is evaporated by heating and rises in the packed bed 11.
On the other hand, the waste sulfuric acid solution is supplied from the supply port 17 and descends in the packed bed. In the packed bed 11, the gas phase and the liquid phase thus form a flow in which they face each other, and a temperature gradient that decreases as they go upward is formed. Then, heat exchange and material transfer are performed between the gas phase and the liquid phase that flow in opposition, as a result, the vapor with a low sulfuric acid concentration rises from the upper surface of the packed bed 11, and the liquid with a high sulfuric acid concentration propagates through the Raschig ring 9. And returns to the storage section 5. The rising vapor is cooled in the cooler 13, part of which is condensed and flows into the packed bed 11, and the rest is liquefied by flowing from the discharge pipe 15 to the condenser 3 and is discharged to the drain as about 5% diluted sulfuric acid. It In the evaporation tower 2, sulfuric acid having a concentration of about 96% is evaporated, reaches the condenser 4 through the packed bed 12 and the cooler 14, and is recovered as a product.
【0006】[0006]
【発明が解決しようとする課題】上記のような装置にお
いて、流下する液量が多い場合、あるいは蒸発した蒸気
量が多い場合などに、充填層11,12内の網状空間が
塞がれて蒸発気体が抜けにくくなり、圧力が上昇してガ
ラス製のラシヒリング9が持ち上げられ、落下して破損
するという事故が起きることがある。このような事故を
防止するには、所定の箇所に逆止弁のような圧抜き手段
を設ければよいが、装置がガラスで構成され、また高度
に腐食性の流体を扱うので、構造やメンテナンスが簡単
な圧抜き手段を構成するのは困難であった。この発明の
目的は、槽内の圧力上昇による事故の発生を簡単な構造
で回避できるような処理槽の安全弁を提供することであ
る。In the above apparatus, when the amount of liquid flowing down is large or the amount of vaporized vapor is large, the reticulated spaces in the packed layers 11 and 12 are closed and vaporized. Gas may become difficult to escape, the pressure may rise, the Raschig ring 9 made of glass may be lifted, and may fall and be damaged. In order to prevent such an accident, a pressure relief means such as a check valve may be provided at a predetermined location, but since the device is made of glass and handles highly corrosive fluid, the structure and It has been difficult to construct a pressure relief means that is easy to maintain. An object of the present invention is to provide a safety valve for a processing tank that can avoid an accident due to a pressure increase in the tank with a simple structure.
【0007】[0007]
【課題を解決するための手段】請求項1に記載の発明
は、容器の所定部分に小片が充填された充填層が構成さ
れ、この充填層に被処理流体を通して所定の処理を行な
うようにした処理槽において、上記充填層には、該充填
層の上下を貫通する圧抜管路が形成され、この圧抜管路
には液溜部が形成されていることを特徴とする処理槽の
安全弁である。請求項2に記載の発明は、上記圧抜管路
がS字状の管で構成されていることを特徴とする請求項
1に記載の処理槽の安全弁である。According to a first aspect of the present invention, a filling layer is formed by filling a predetermined portion of a container with small pieces, and a fluid to be treated is passed through the filling layer to perform a predetermined treatment. In the processing tank, a pressure relief pipe line is formed in the packed bed so as to pass through the packed bed vertically, and a liquid reservoir is formed in the pressure relief pipe path. . The invention according to claim 2 is the safety valve for a processing tank according to claim 1, characterized in that the depressurizing conduit is constituted by an S-shaped pipe.
【0008】請求項3に記載の発明は、圧抜管路の上側
開口部の近傍に、被処理流体をこの開口部に導く導入構
造が構成されていることを特徴とする請求項1又は2に
記載の処理槽の安全弁である。これは、例えば、開口部
を末広がりに形成する、開口部を容器の壁に接して設け
る、開口部の上部に流体を滴下するような突起を形成す
るなどの方法が採用される。請求項4に記載の発明は、
上記小片及び/又は圧抜管路が、ガラスから形成されて
いることを特徴とする請求項1ないし3のいずれかに記
載の処理槽の安全弁である。The invention according to claim 3 is characterized in that an introduction structure for guiding the fluid to be treated to this opening is formed in the vicinity of the upper opening of the depressurizing conduit. This is a safety valve for the processing tank described. For this, for example, a method of forming the opening in a divergent manner, providing the opening in contact with the wall of the container, or forming a projection for dropping a fluid on the upper portion of the opening is adopted. The invention described in claim 4 is
The safety valve for a processing tank according to any one of claims 1 to 3, wherein the small piece and / or the depressurizing pipe line is made of glass.
【0009】請求項5に記載の発明は、上記処理槽が、
流体を加熱して分留する精製装置であることを特徴とす
る請求項1ないし4のいずれかに記載の処理槽の安全弁
である。請求項6に記載の発明は、上記処理槽が、流体
を加熱して蒸発させる蒸発装置であることを特徴とする
請求項1ないし4のいずれかに記載の処理槽の安全弁で
ある。請求項7に記載の発明は、上記流体が硫酸である
ことを特徴とする請求項5又は6に記載の処理槽の安全
弁である。According to a fifth aspect of the present invention, the processing tank comprises:
The safety valve for a processing tank according to any one of claims 1 to 4, which is a refining device for heating and fractionating a fluid. The invention according to claim 6 is the safety valve for a processing tank according to any one of claims 1 to 4, wherein the processing tank is an evaporator that heats and evaporates a fluid. The invention according to claim 7 is the safety valve for a processing tank according to claim 5 or 6, characterized in that the fluid is sulfuric acid.
【0010】[0010]
【作用】請求項1に記載の発明においては、充填層の上
下において所定以上の差圧が発生すると、圧抜管路の液
溜部に溜まった液の圧力に逆らって流体が流れ、それに
より差圧を緩和する。請求項2に記載の発明において
は、液溜部が圧抜管の一部をS字状に形成することによ
り容易に構成される。According to the present invention, when a pressure difference above and below the packed bed exceeds a predetermined level, the fluid flows against the pressure of the liquid accumulated in the liquid reservoir of the depressurizing pipe line, thereby causing a difference. Relieve pressure. In the invention described in claim 2, the liquid reservoir is easily configured by forming a part of the depressurizing tube in an S shape.
【0011】請求項3に記載の発明においては、被処理
流体が導入構造により開口部に導かれ、自然に液溜部に
液が溜められる。請求項4に記載の発明においては、上
記小片及び/又は圧抜管路は、ガラスから形成され、被
処理流体に対する耐食性が向上する。請求項5に記載の
発明においては、処理槽の下側で流体が加熱され、処理
槽中を上昇し、その過程で分留されて精製される。請求
項6に記載の発明においては、処理槽の下側で流体が加
熱されて処理槽中を上昇し、不揮発性成分との分離が行
われて精製される。請求項7に記載の発明においては、
硫酸が分留されて精製される。In the third aspect of the invention, the fluid to be treated is guided to the opening by the introduction structure, and the liquid is naturally accumulated in the liquid reservoir. In the invention according to claim 4, the small piece and / or the depressurizing pipe line is formed of glass, and the corrosion resistance to the fluid to be treated is improved. In the invention according to claim 5, the fluid is heated under the treatment tank, rises in the treatment tank, and is fractionated and purified in the process. In the sixth aspect of the invention, the fluid is heated under the treatment tank to rise in the treatment tank, and is separated from the non-volatile components to be purified. In the invention according to claim 7,
Sulfuric acid is fractionated and purified.
【0012】[0012]
【実施例】図1は、この発明の一実施例の処理槽の安全
弁を示すもので、従来と同様の部分は符号を同じくして
説明を省略する。この実施例では、充填層11,12
に、この充填層の上流と下流を挿通する圧抜管21,2
2が小片を保持する枠体に取り付けられている。この圧
抜管21,22は、ガラス製のS字管として形成され、
それによって液溜部23,24が形成されている。この
圧抜管は、上端が上広がりのロート部25,26に形成
されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a safety valve of a processing tank according to an embodiment of the present invention. The same parts as in the prior art are designated by the same reference numerals and the description thereof will be omitted. In this embodiment, the packing layers 11, 12 are
And the pressure-removing pipes 21 and 2 inserted through the upstream and downstream of the packed bed.
2 is attached to the frame that holds the pieces. The depressurization tubes 21 and 22 are formed as glass S-shaped tubes,
As a result, liquid reservoirs 23 and 24 are formed. The depressurizing tube is formed with funnel portions 25 and 26 whose upper ends are widened upward.
【0013】濃縮塔1の圧抜管21はその縁を容器の内
壁1aに接するようにして取付られている。S字状の圧
抜管21,22の重複する部分の高さh(図2参照)
は、この安全弁が作動する圧力などに応じて設定され
る。また、圧抜管21,22の太さは、通常の稼動状態
であれば圧抜管21,22に流入した液が差圧で押し出
されず、蒸気と液が置き換わる程度に、そして、所定の
圧力上昇があった場合には、液を押し出して蒸気が抜け
ることができるように設定する。The depressurizing tube 21 of the concentrating tower 1 is attached so that its edge contacts the inner wall 1a of the container. Height h of the overlapping portions of the S-shaped depressurization tubes 21 and 22 (see FIG. 2)
Is set according to the pressure at which this safety valve operates. Further, the thickness of the depressurizing pipes 21 and 22 is such that, in a normal operating state, the liquid flowing into the depressurizing pipes 21 and 22 is not pushed out by the differential pressure, and the vapor and the liquid are replaced with each other, and the predetermined pressure rise is achieved. If there is, set it so that the liquid can be pushed out and vapor can escape.
【0014】このように構成された処理槽の安全弁の作
用を濃縮塔1について説明する。濃縮塔1の冷却器13
の周囲の壁1aから冷却された液が伝って降下し、圧抜
管21に流入するので、圧抜管21の液溜部23には常
に高さhの液溜まりが自然に形成される。正常動作時に
おいては、蒸気は液溜部23に阻止されるので圧抜管2
1を通って上側に流出することはない。貯留部5におけ
る圧力が上昇した場合には図2(b)に示すように液溜
部23の平衡が崩れ、さらに、その圧力が圧抜管21の
液溜部23の高さhの2倍によって決まる圧力を超えた
ところで、図2(c)に示すように貯留部5の蒸気がこ
の圧抜管21を通って噴出する。これによって、圧力の
異常上昇が抑えられ、充填層11の小片が上下動して破
損するなどの事故が防止される。液溜部23は自然に形
成されるので、特に液溜を形成する作業を必要としな
い。The operation of the safety valve of the processing tank thus constructed will be described with respect to the concentration tower 1. Cooling device 13 of the concentration tower 1
The cooled liquid is transmitted from the surrounding wall 1a and descends and flows into the depressurizing pipe 21, so that the liquid reservoir 23 of the depressurizing pipe 21 always naturally forms a liquid reservoir having a height h. During normal operation, vapor is blocked by the liquid reservoir 23, so the depressurizing pipe 2
It does not flow through 1 to the upper side. When the pressure in the storage part 5 rises, the equilibrium of the liquid storage part 23 is disrupted as shown in FIG. 2 (b), and the pressure becomes twice the height h of the liquid storage part 23 of the depressurization pipe 21. When the determined pressure is exceeded, the vapor in the reservoir 5 is ejected through the depressurization pipe 21 as shown in FIG. 2 (c). This suppresses an abnormal increase in pressure, and prevents an accident such as a small piece of the packed bed 11 moving up and down and being damaged. Since the liquid reservoir 23 is formed naturally, the work for forming the liquid reservoir is not required.
【0015】図3は、蒸発塔2の安全弁の構造を示すも
ので、冷却器14に下方に突出する突起27を形成し、
その突起27の下側に圧抜管22を開口させるようにし
たものである。この実施例によれば、冷却器14で凝縮
した液体の一部が常に圧抜管22に流入するので、一定
量の液溜がより安定的に維持される。FIG. 3 shows the structure of the safety valve of the evaporation tower 2, in which the protrusion 27 protruding downward is formed on the cooler 14.
The depressurization tube 22 is opened below the protrusion 27. According to this embodiment, a part of the liquid condensed in the cooler 14 always flows into the depressurizing pipe 22, so that a constant amount of the liquid reservoir is maintained more stably.
【0016】なお、本発明の実施は上記の態様に限られ
るものではなく、使用される処理槽の種類は例えば濾過
装置などに用いてもよく、また、各部材の材質、充填さ
れる小片の形状、寸法、圧抜管の液溜部の形状などは適
宜のものが使用されてよい。また、液溜部を構成するS
字管を、図2(d)及び(e)にに示すように、重複部
を結合した結合管21aとすることにより、省スペース
化と強度の向上を図るようにしてもよい。The embodiment of the present invention is not limited to the above-described embodiment, and the type of the processing tank used may be, for example, a filtering device, the material of each member, and the small pieces to be filled. Any appropriate shape, size, shape of the liquid reservoir of the depressurization tube, and the like may be used. In addition, S that constitutes the liquid reservoir
As shown in FIGS. 2 (d) and 2 (e), the character tube may be a coupling tube 21a in which overlapping portions are coupled to each other to save space and improve strength.
【0017】[0017]
【発明の効果】請求項1に記載の発明によれば、充填層
の上下における差圧が自動的に緩和され、槽内の圧力上
昇による事故の発生を簡単な構造で回避することができ
る。構造が簡単なので、ガラスのような耐食性材料で作
成することができ、腐食性流体の処理にも適用が容易で
ある。構造が簡単であること、通常自然に流体が液溜部
に溜まることから、メンテナンスも容易である。請求項
2に記載の発明によれば、液溜部が圧抜管の一部をS字
状に曲げるだけで製造でき、コストが安い。According to the first aspect of the present invention, the pressure difference between the upper and lower sides of the packed bed is automatically relieved, and the occurrence of an accident due to the pressure increase in the tank can be avoided with a simple structure. Due to its simple structure, it can be made of a corrosion resistant material such as glass, and is easily applied to the treatment of corrosive fluids. Maintenance is easy because the structure is simple and the fluid normally accumulates in the liquid reservoir. According to the invention as set forth in claim 2, the liquid reservoir can be manufactured only by bending a part of the depressurizing tube into an S shape, and the cost is low.
【0018】請求項3に記載の発明においては、導入構
造により自然に液溜部に液が溜められるので、メンテナ
ンスが容易である。請求項4に記載の発明においては、
上記小片及び/又は圧抜管路がガラスから形成され、腐
食性の高い被処理流体の処理に適用できる。請求項5に
記載の発明においては、被処理流体の分留・精製工程が
安定に行われ、能率の向上とコストの低下をもたらす。
請求項6に記載の発明においては、被処理流体を蒸発さ
せて精製する工程が安定に行われ、能率の向上とコスト
の低下をもたらす。請求項7に記載の発明においては、
硫酸の分留・精製工程が安定に行われ、能率の向上とコ
ストの低下をもたらす。According to the third aspect of the invention, since the liquid is naturally accumulated in the liquid reservoir by the introduction structure, the maintenance is easy. In the invention of claim 4,
The above-mentioned small piece and / or the depressurizing pipe line are formed from glass, and can be applied to the treatment of a highly corrosive fluid to be treated. In the invention described in claim 5, the process of fractionating and refining the fluid to be treated is stably performed, resulting in an improvement in efficiency and a reduction in cost.
In the invention described in claim 6, the step of evaporating and purifying the fluid to be processed is stably performed, which improves the efficiency and reduces the cost. In the invention according to claim 7,
Sulfuric acid fractionation / purification process is performed stably, resulting in improved efficiency and cost reduction.
【図1】この発明の一実施例の硫酸回収装置の模式図で
ある。FIG. 1 is a schematic diagram of a sulfuric acid recovery apparatus according to an embodiment of the present invention.
【図2】この発明の一実施例の圧抜管における動作を示
す図である。FIG. 2 is a view showing the operation of the pressure relief pipe according to the embodiment of the present invention.
【図3】この発明の他の実施例の圧抜管における動作を
示す図である。FIG. 3 is a view showing the operation of the pressure relief pipe of another embodiment of the present invention.
【図4】この発明に用いる充填槽の小片の例を示す図で
ある。FIG. 4 is a diagram showing an example of a small piece of a filling tank used in the present invention.
【図5】従来の硫酸回収装置の模式図である。FIG. 5 is a schematic view of a conventional sulfuric acid recovery device.
1 濃縮塔(容器) 2 蒸発塔(容器) 9,9a,9b ラシヒリング(小片) 11,12 充填層 21,21a,22 圧抜管 23,24 液溜部 25,26 ロート部 27 突起 1 Concentration Tower (Container) 2 Evaporation Tower (Container) 9, 9a, 9b Raschig Ring (Small Piece) 11, 12 Packed Bed 21, 21a, 22 Depressurization Tube 23, 24 Liquid Reservoir 25, 26 Funnel 27 Protrusion
Claims (7)
層が構成され、この充填層に被処理流体を通して所定の
処理を行なうようにした処理槽において、 上記充填層には、該充填層の上下を貫通する圧抜管路が
形成され、この圧抜管路には液溜部が形成されているこ
とを特徴とする処理槽の安全弁。1. A treatment tank in which a predetermined layer of a container is filled with small pieces to form a filling layer, and a predetermined treatment is carried out by passing a fluid to be treated through the filling layer, wherein the filling layer has the filling layer. A safety valve for a processing tank, characterized in that a pressure release pipe line is formed so as to pass through the upper and lower sides of the container and a liquid reservoir is formed in the pressure release pipe line.
いることを特徴とする請求項1に記載の処理槽の安全
弁。2. The safety valve for a processing tank according to claim 1, wherein the depressurizing pipe line is composed of an S-shaped pipe.
理流体をこの開口部に導く導入構造が構成されているこ
とを特徴とする請求項1又は2に記載の処理槽の安全
弁。3. The safety valve for a treatment tank according to claim 1, wherein an introduction structure for guiding the fluid to be treated to the opening is formed in the vicinity of the upper opening of the depressurizing pipe line. .
から形成されていることを特徴とする請求項1ないし3
のいずれかに記載の処理槽の安全弁。4. The small piece and / or the depressurizing pipe line are made of glass.
The safety valve for the processing tank according to any one of 1.
精製装置であることを特徴とする請求項1ないし4のい
ずれかに記載の処理槽の安全弁。5. The safety valve for a processing tank according to claim 1, wherein the processing tank is a refining device for heating and fractionating a fluid.
る蒸発装置であることを特徴とする請求項1ないし4の
いずれかに記載の処理槽の安全弁。6. The safety valve for a processing tank according to claim 1, wherein the processing tank is an evaporator that heats and evaporates a fluid.
請求項5又は6に記載の処理槽の安全弁。7. The safety valve for a processing tank according to claim 5, wherein the fluid is sulfuric acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20833495A JPH0942501A (en) | 1995-07-24 | 1995-07-24 | Safety valve for treating vessel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20833495A JPH0942501A (en) | 1995-07-24 | 1995-07-24 | Safety valve for treating vessel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0942501A true JPH0942501A (en) | 1997-02-14 |
Family
ID=16554557
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20833495A Pending JPH0942501A (en) | 1995-07-24 | 1995-07-24 | Safety valve for treating vessel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0942501A (en) |
-
1995
- 1995-07-24 JP JP20833495A patent/JPH0942501A/en active Pending
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