JPH0857292A - Packed column - Google Patents

Packed column

Info

Publication number
JPH0857292A
JPH0857292A JP19515294A JP19515294A JPH0857292A JP H0857292 A JPH0857292 A JP H0857292A JP 19515294 A JP19515294 A JP 19515294A JP 19515294 A JP19515294 A JP 19515294A JP H0857292 A JPH0857292 A JP H0857292A
Authority
JP
Japan
Prior art keywords
liquid
packed column
packed
packing material
gas
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
Application number
JP19515294A
Other languages
Japanese (ja)
Inventor
Yukiyoshi Yoshimatsu
幸祥 吉松
Susumu Harada
原田  進
Shigeyasu Okamoto
成恭 岡本
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP19515294A priority Critical patent/JPH0857292A/en
Publication of JPH0857292A publication Critical patent/JPH0857292A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/3221Corrugated sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32213Plurality of essentially parallel sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32224Sheets characterised by the orientation of the sheet
    • B01J2219/32227Vertical orientation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32237Sheets comprising apertures or perforations

Landscapes

  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE: To reduce pressure loss and to widen an operation range by smoothing the flowing-down of a liquid from the corrugated groove of a packing material. CONSTITUTION: This packed column is constituted so as to have such a structure that the lower end 11 of the packing material at the lowerst part of a packed bed constituted at every block is arranged at the position being in contact with the surface 21 of the liquid present in the lower part of the column or at least immersed in the liquid. By this constitution, since the liquid continuously flows out of the lower end part of the packing material at the lowermost part of the packed bed, the packed column reduced in pressure loss and wide in an operation range can be provided.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、充填材を充填した充填
塔に関し、特に空気分離装置において、空気から酸素,
窒素,アルゴン等を精留する精留塔及び、空気圧縮機か
らの空気を冷却する水洗冷却塔、該水洗冷却塔の水を冷
却する蒸発冷却塔に適した充填塔に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a packed column packed with a packing material, and particularly in an air separation device,
The present invention relates to a rectification column for rectifying nitrogen, argon, etc., a water washing cooling tower for cooling air from an air compressor, and a packed tower suitable for an evaporative cooling tower for cooling water of the water washing cooling tower.

【0002】[0002]

【従来の技術】充填塔は、蒸留,精留,吸収操作等の化
学工学の分野で幅広く用いられている。そして充填材に
は、ラシヒリング,テラレットに代表される不規則型充
填材が、安価で取扱が容易なため広く用いられている
が、実開平3-128281号公報に見られるように、充填材中
を流れる液体及びガスの分散性に問題がある。一方、メ
ラパック(スルザー社)等に代表される規則型充填物は、
充填材自体がある程度の液体及びガスの分散性を有する
ため、最近各分野に普及し始めている。
2. Description of the Related Art A packed column is widely used in the field of chemical engineering such as distillation, rectification and absorption operation. Irregular fillers such as Raschig rings and terraret are widely used as fillers because they are cheap and easy to handle, but as shown in Japanese Utility Model Publication No. 3-128281, There is a problem with the dispersibility of liquids and gases flowing through. On the other hand, the regular packing represented by Melapak (Sulzer), etc.
Since the filler itself has a certain degree of liquid and gas dispersibility, it has recently become popular in various fields.

【0003】本発明は、上記後者の充填材を対象とした
ものである。この種の装置に関するものとしては、特公
昭57-36009号公報,特開昭61-291017号公報等に記載さ
れたものが挙げられる。これらの内容は、充填材自体の
構造に関するものであり、充填材を充填した充填塔とし
ての構造としては、例えば、特開昭56-155601号公報に
記載されたものがある。しかしながら、これら従来の技
術においては、充填材中の液体の流れまでを考慮した充
填塔の構造とはなっていなかった。
The present invention is directed to the latter filling material. Examples of this type of device include those described in Japanese Patent Publication No. 57-36009, Japanese Patent Laid-Open No. 61-291017, and the like. These contents are related to the structure of the packing material itself, and as a structure of the packed column packed with the packing material, there is, for example, one described in JP-A-56-155601. However, in these conventional techniques, the structure of the packed column has not been taken into consideration even the flow of the liquid in the packing material.

【0004】また、空気の分離における充填材の適用に
ついては、INDUSTRYAL AND ENGINEERING CHEMISTRY Vo
l.39,No.6にて、窒素、酸素系について検討を行ってい
る。
Regarding the application of the filler in separating air, INDUSTRYAL AND ENGINEERING CHEMISTRY Vo
In l.39, No.6, we are studying nitrogen and oxygen systems.

【0005】[0005]

【発明が解決しようとする課題】充填材を内蔵した充填
塔では、互いに接触する気相と液相の気液接触の効率
が、充填材の表面積の大小に影響する。特に、高い分離
性能を要求する場合、できるだけ大きな表面積を有した
方が効果的である。このためには、充填材の単位体積あ
たりの表面積を大きくして、全体の表面積を大きくする
方法がある。この方法は、充填材を構成する薄層物波形
溝のピッチを小さくすることで、単位体積あたりの表面
積を大きくする方法である。
In a packed column containing a packing material, the efficiency of gas-liquid contact between the gas phase and the liquid phase in contact with each other affects the size of the surface area of the packing material. Especially when high separation performance is required, it is effective to have a surface area as large as possible. For this purpose, there is a method of increasing the surface area of the filler per unit volume to increase the total surface area. This method is a method of increasing the surface area per unit volume by reducing the pitch of the thin layer corrugated grooves constituting the filling material.

【0006】しかしながら、薄層物波形溝のピッチを小
さくすると、波形溝の断面積が減少することになる。充
填材は、波形溝を介してガスや液が上昇,下降するもの
であるから、断面積の減少は少なからず下降する液体の
滞留を引き起こす。すなわち、液体の表面張力,粘性,
密度等の影響により、液体がブロック毎に構成される充
填材の下端の波形溝より自由に下方へ流下しなくなる。
この現象は、前記充填材の下端で起こり、波形溝が見か
け上液体の膜で覆われ、さらに液体は部分的に落下す
る。この液体の膜を打ち破るためにガスの圧力損失が増
大し、さらにローディグ現象を引き起して充填塔は不安
定な操作となり、結果的には、運転操作範囲が狭くなる
という問題があった。
However, when the pitch of the thin-layer corrugated grooves is reduced, the cross-sectional area of the corrugated grooves is reduced. Since the gas and the liquid rise and fall through the corrugated groove in the filling material, the decrease in the cross-sectional area causes a considerable amount of descent liquid retention. That is, liquid surface tension, viscosity,
Due to the influence of the density and the like, the liquid does not freely flow downward from the corrugated groove at the lower end of the filling material formed for each block.
This phenomenon occurs at the lower end of the filling material, the corrugated grooves are apparently covered with a film of liquid, and the liquid partially drops. There was a problem that the pressure loss of the gas increased due to the breakage of the liquid film, and further, the Rhodig phenomenon was caused to cause unstable operation of the packed column, resulting in a narrow operating range.

【0007】本発明の目的は、圧力損失の低減及び運転
操作範囲の広範囲化を可能とする充填塔を提供すること
にある。
An object of the present invention is to provide a packed column capable of reducing pressure loss and widening the operation range.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
には、充填材中を上方から流下する液体を、ブロック毎
に充填してある充填材の最下部より滑らかに流下させる
必要があり、そのための手段として、充填塔内の各ブロ
ック毎に構成された最下部の充填材の下端を少なくとも
その下方にある液体の液面に接する構造とすることで達
成される。
In order to achieve the above object, it is necessary that the liquid flowing down from above in the filler is made to flow smoothly from the lowermost portion of the filler filled in each block, As a means therefor, it is achieved by providing a structure in which the lower end of the lowermost packing material formed for each block in the packed column is in contact with at least the liquid surface of the liquid therebelow.

【0009】[0009]

【作用】充填塔内の最下部の充填材の下端を下方にある
液体の液面に接するようにすることにより、最下部の充
填材を流出する液体は、見かけ上、下方にある液体と連
続した格好となり、この連続した液体の作用により液体
は滑らかに下方へ流出する。このため、充填材の最下部
の波形溝が液体の膜で覆われることが無くなり、この結
果、圧力損失の増加の現象も無くなり、ひいては、運転
操作範囲の広いコンパクトな充填塔を提供できる。
By allowing the lower end of the lowermost packing material in the packed column to contact the liquid surface of the lower liquid, the liquid flowing out of the lowermost packing material is apparently continuous with the lower liquid. The liquid smoothly flows downward due to the continuous action of the liquid. Therefore, the corrugated groove at the bottom of the packing material is not covered with the liquid film, and as a result, the phenomenon of increase in pressure loss is also eliminated, and as a result, a compact packed column having a wide operating range can be provided.

【0010】[0010]

【実施例】以下、本発明の第一の実施例を図面に基づい
て説明する。図1は本発明の充填塔の縦断面図を示す。
充填塔100は、空気から酸素,窒素,アルゴン等を分
離する精留塔を例に説明する。空気分離装置で使用され
る主精留塔では、低圧力で操作する上塔1、高圧力で操
作する下塔2、及び液体酸素3を蒸発させ下塔の上部か
らの窒素ガス4を凝縮させる主凝縮器5により構成され
る。上塔1内には、充填材6〜8が各ブロック毎に塔軸
方向に積み重ねて設置してある。各々の充填材は、例え
ば充填材6と7は、該充填材の構成要素である薄層要素
に対して90度ずつずらされて塔軸方向に設置してあ
る。また、薄層要素表面には、微小波形溝9を有してい
る。各々の充填材6〜8はその外周に巻かれた帯10に
より一体に固定され、さらに該帯10の先端は折り曲げ
て上塔1に固定されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows a vertical sectional view of a packed tower of the present invention.
The packed column 100 will be described by taking a rectification column that separates oxygen, nitrogen, argon, etc. from air as an example. In the main rectification column used in the air separation device, an upper column 1 operated at a low pressure, a lower column 2 operated at a high pressure, and liquid oxygen 3 are evaporated to condense nitrogen gas 4 from the upper part of the lower column. It is composed of the main condenser 5. Fillers 6 to 8 are installed in the upper tower 1 in a stacked manner in the axial direction of each block for each block. Each of the fillers, for example, the fillers 6 and 7 is installed in the column axis direction by being shifted by 90 degrees with respect to the thin layer element which is a constituent element of the filler. Further, the thin layer element surface has minute corrugated grooves 9. Each of the fillers 6 to 8 is integrally fixed by a band 10 wound around the outer periphery thereof, and the tip of the band 10 is bent and fixed to the upper tower 1.

【0011】本発明の特徴である各ブロック毎に設置さ
れた充填材の最下部のブロックの設置方法は、本例の場
合、充填材6は、その下端11がその下方にある液体酸
素3の液面21に接し、あるいは、埋没して構成されて
いる。もちろん、最下部の充填材6は、上塔の筐体12
より、例えば補強等(図示せず)により支えられてい
る。図1に示すように、精留塔の上塔1の上方から流下
する液体20は、充填材8,7,6の順に流下し、上昇
ガス30は、主凝縮器5により液体酸素3を蒸発させる
ことにより空間31より上昇し、各ブロックの少なくと
も充填材6の側面から充填材6中に流入して上昇する。
前記充填材表面で気液接触を行い、液,ガスの分離を行
う。主凝縮器5で液体酸素3と熱交換した窒素ガス4
は、液体窒素40となり、下塔2に還流液として導入さ
れる。
The method of installing the lowermost block of the packing material installed in each block, which is a feature of the present invention, is that in the case of this example, the packing material 6 has a lower end 11 of liquid oxygen 3 below it. It is configured to be in contact with the liquid surface 21 or to be buried therein. Of course, the filling material 6 at the bottom is the casing 12 of the upper tower.
Therefore, it is supported by, for example, reinforcement (not shown). As shown in FIG. 1, the liquid 20 flowing down from above the upper tower 1 of the rectification tower flows down in the order of the packing materials 8, 7 and 6, and the rising gas 30 vaporizes the liquid oxygen 3 by the main condenser 5. By doing so, it rises from the space 31 and flows into the filling material 6 from at least the side surface of the filling material 6 of each block and rises.
Gas-liquid contact is performed on the surface of the filling material to separate liquid and gas. Nitrogen gas 4 that exchanged heat with liquid oxygen 3 in the main condenser 5
Becomes liquid nitrogen 40 and is introduced into the lower tower 2 as a reflux liquid.

【0012】前述したごとく、充填材の分離性能を高く
するために、充填材の波形溝の断面積を小さくし単位体
積あたりの表面積を大きくした場合、上方からの液体の
量が多くなれば液体の表面張力,粘性,密度等の影響に
より、液体が充填材6の下端より滑らかに流下できなく
なる場合がある。
As described above, in order to improve the separating performance of the packing material, when the cross-sectional area of the corrugated groove of the packing material is made small and the surface area per unit volume is made large, if the amount of liquid from above increases The liquid may not be able to flow smoothly from the lower end of the filling material 6 due to the influence of the surface tension, viscosity, density, and the like.

【0013】本発明では、充填材6は、その下端11が
その下方にある液体酸素3の液面に接し、あるいは、埋
没して構成されているため、充填材6から流出する液体
は連続的に液体酸素3中に流入することができる。した
がって、該充填材6の下部の波形溝は見かけ上液体の膜
で覆われることがなくなるため、圧力損失の増加、ある
いは、ローディング現象を防止でき、さらには、充填塔
の運転操作範囲を広範囲とすることができる。
In the present invention, the lower end 11 of the filling material 6 is in contact with the liquid surface of the liquid oxygen 3 located below the filling material 6 or is buried therein. Therefore, the liquid flowing out from the filling material 6 is continuous. Can flow into the liquid oxygen 3. Therefore, since the corrugated groove below the packing material 6 is apparently not covered with the liquid film, an increase in pressure loss or a loading phenomenon can be prevented, and further, the operation range of the packed column can be widened. can do.

【0014】図2に、本発明の第二の実施例である充填
塔の縦断面図を示す。本実施例では、ブロック毎に設置
された充填材の最下部のブロックの充填材6の下方に、
多数の小孔50を有し上方が開口の液受け皿51を設置
したものである。該液受け皿51は、充填材6の下端1
1と接し、あるいは、隙間52を有して設置される。上
方からの液体20は充填塔6の下端11に達し、液受け
皿51内に流入する。液体20は、液受け皿51に少な
くとも液面22を有し、小孔50を介して下方へ流出す
る。したがって、充填材6の下端は、液体の液面に接
し、あるいは、埋没した格好となり、結果的には、充填
材6の下部の状態は、第一の実施例と同様となり、最下
部の充填材の下端から液体を連続的に滑らかに流出でき
る。また、第一の実施例に比べスペースを有効利用で
き、簡易な方法で圧力損失の増加,ローディング現象を
防止でき、さらには、充填塔の運転操作範囲を広範囲と
することができる効果がある。
FIG. 2 shows a vertical sectional view of a packed column which is a second embodiment of the present invention. In this embodiment, below the filler 6 in the lowermost block of the filler installed for each block,
A liquid receiving tray 51 having a large number of small holes 50 and an opening at the top is installed. The liquid receiving tray 51 is the lower end 1 of the filling material 6.
It is installed so as to be in contact with 1 or have a gap 52. The liquid 20 from above reaches the lower end 11 of the packed tower 6 and flows into the liquid receiving tray 51. The liquid 20 has at least the liquid surface 22 in the liquid receiving tray 51, and flows out downward through the small holes 50. Therefore, the lower end of the filling material 6 is in contact with the liquid surface of the liquid or is buried therein. As a result, the state of the lower portion of the filling material 6 is the same as that of the first embodiment, and the filling of the lowermost portion is performed. Liquid can be continuously and smoothly discharged from the lower end of the material. Further, compared with the first embodiment, the space can be effectively used, the pressure loss can be prevented from increasing and the loading phenomenon can be prevented by a simple method, and further, the operation range of the packed column can be widened.

【0015】本実施例において、液受け皿51の小孔5
0を有さない場合、液体20は、液受け皿51を構成す
る側板53を溢れ出て下方へ流出する。本例の場合も、
第一の実施例と同様の効果を得ることができる。
In this embodiment, the small hole 5 of the liquid receiving tray 51
When it does not have 0, the liquid 20 overflows the side plate 53 that constitutes the liquid receiving tray 51 and flows out downward. Also in this example,
The same effect as that of the first embodiment can be obtained.

【0016】図3に、本発明の第三の実施例である充填
塔の縦断面図を示す。本実施例では、第二の実施例の構
造を、充填塔100の他の場所に適用したものである。
充填塔100内の充填材は、ブロック毎に十数段積み重
ねられ、連続した充填材として構成され、これらを組み
合わせて充填塔として構成される。したがって、ブロッ
ク毎に構成された最下部の充填材は、充填塔100内に
数個所存在することになる。充填塔100の上方から該
充填塔内に設置された充填材7,6を流下した液体20
は、充填材6の下端11に達し、液受け皿51内に流入
する。液体20は、液受け皿51に少なくとも液面22
を有し、小孔50を介して下方へ流出する。したがっ
て、充填材6の下端は、液体の液面22に接し、あるい
は、埋没した格好となり、液受け皿51,小孔50を介
して下方の充填材60,70に流入する。このため、最
下部の充填材の下端から液体を連続的に滑らかに流出で
きる。したがって、第一の実施例に比べスペースを有効
利用でき、簡易な方法で圧力損失の増加,ローディング
現象を防止でき、さらには、充填塔の運転操作範囲を広
範囲とすることができる効果がある。液受け皿51は、
小孔50を介して液体20を下方へ分散させて流出させ
る液分配器の作用も成すが、さらに分配能力を高めるた
めに液受け皿51と充填材60の間には必要に応じて液
分配器等が設置される。また、本実施例の筐体12は空
間31を有し、上昇ガス30を上昇させるに必要な程度
大きな構造となる。下方からの上昇ガス30は空間31
を介して上昇し、各ブロックの少なくとも充填材6の側
面から充填材中に流入し、上昇する。本実施例では、第
二の実施例の構造を、充填塔の他の場所に適用したもの
であり、第一及び第二の実施例と同様の効果を得ること
ができる。
FIG. 3 shows a vertical sectional view of a packed tower which is a third embodiment of the present invention. In this embodiment, the structure of the second embodiment is applied to another place of the packed column 100.
The packing material in the packed tower 100 is stacked for each block in a dozen or more stages to form a continuous packing material, and these are combined to form a packed tower. Therefore, the lowermost packing material configured for each block is present in several places in the packed tower 100. A liquid 20 that has flowed down the packing materials 7 and 6 installed in the packed tower 100 from above the packed tower 100.
Reaches the lower end 11 of the filling material 6 and flows into the liquid receiving tray 51. The liquid 20 is placed on the liquid pan 51 at least on the liquid surface 22.
And flows downward through the small hole 50. Therefore, the lower end of the filling material 6 comes into contact with the liquid surface 22 of the liquid or is buried therein, and flows into the lower filling materials 60 and 70 through the liquid receiving tray 51 and the small holes 50. Therefore, the liquid can be continuously and smoothly discharged from the lower end of the lowermost filler. Therefore, as compared with the first embodiment, the space can be effectively used, the pressure loss can be increased and the loading phenomenon can be prevented by a simple method, and further, the operation range of the packed column can be widened. The liquid tray 51 is
It also acts as a liquid distributor that causes the liquid 20 to be dispersed downward through the small holes 50 and flows out. However, in order to further enhance the distribution ability, a liquid distributor may be provided between the liquid receiving tray 51 and the filling material 60 as needed. Etc. are installed. Further, the housing 12 of this embodiment has a space 31 and has a structure large enough to raise the rising gas 30. Ascending gas 30 from below is space 31
Rises through at least the side surface of the filler 6 of each block, flows into the filler, and rises. In this embodiment, the structure of the second embodiment is applied to another place of the packed column, and the same effect as that of the first and second embodiments can be obtained.

【0017】[0017]

【発明の効果】本発明によれば、充填塔内の各ブロック
毎に構成された最下部の充填材の下端を下方にある液体
の液面に少なくとも接することにより、上方からの液体
を充填塔内の最下部の充填材の波形溝から滑らかに流出
させることができる。この結果、圧力損失が少なく、運
転操作範囲の広い充填塔を提供できる効果がある。
According to the present invention, the liquid from above is packed by contacting at least the lower end of the lowermost packing material for each block in the packed tower with the liquid surface of the liquid below. It is possible to smoothly flow out from the corrugated groove of the lowermost filling material. As a result, there is an effect that a packed column with a small pressure loss and a wide operation range can be provided.

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

【図1】本発明の第一の実施例を示す充填塔の縦断面図
である。
FIG. 1 is a vertical sectional view of a packed tower showing a first embodiment of the present invention.

【図2】本発明の第二の実施例を示す充填塔の縦断面図
である。
FIG. 2 is a vertical sectional view of a packed tower showing a second embodiment of the present invention.

【図3】本発明の第三の実施例を示す充填塔の縦断面図
である。
FIG. 3 is a vertical sectional view of a packed tower showing a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

6,7,8,60,70…充填材、21…液面、11…
充填材の下端、20…液体、30…上昇ガス、50…小
孔、51…液受け皿、100…充填塔。
6, 7, 8, 60, 70 ... Filler, 21 ... Liquid level, 11 ...
The lower end of the packing material, 20 ... Liquid, 30 ... Ascending gas, 50 ... Small hole, 51 ... Liquid pan, 100 ... Packing tower.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】複数の充填材が軸方向に多段設置され、各
充填材は、充填塔内に平行に配置された波形溝を有する
複数の薄層物によって構成され、隣接する薄層物はそれ
らの波形溝が互いに交差するように配置され、かつ、該
薄層物は間隔をおいて配置された小孔の列を有し、上部
から液体を流下させ、該液体と下部から上昇する気体と
を向交流接触させる気液接触用の充填塔において、複数
のブロックで構成された充填材の最下部のブロックの充
填材の下端部が、その下方にある液体の液面に接する位
置、あるいは、埋没する位置に設置される構造としたこ
とを特徴とする充填塔。
1. A plurality of packing materials are installed in multiple stages in the axial direction, each packing material is constituted by a plurality of thin layer products having corrugated grooves arranged in parallel in a packed column, and adjacent thin layer products are A gas in which the corrugated grooves are arranged so as to intersect with each other, and the thin layered article has rows of small holes arranged at intervals so that the liquid flows down from the upper part and rises from the liquid and the lower part. In a gas-liquid contacting packed column for making a direct alternating current contact with each other, the lower end of the filler in the lowermost block of the filler composed of a plurality of blocks is in contact with the liquid surface of the liquid thereunder, or A packed tower characterized by having a structure installed at a position to be buried.
【請求項2】複数の充填材が軸方向に多段設置され、各
充填材は、充填塔内に平行に配置された波形溝を有する
複数の薄層物によって構成され、隣接する薄層物はそれ
らの波形溝が互いに交差するように配置され、かつ、該
薄層物は間隔をおいて配置された小孔の列を有し、上部
から液体を流下させ、該液体と下部から上昇する気体と
を向交流接触させる気液接触用の充填塔において、複数
のブロックで構成された充填材の最下部のブロックの充
填材の下方に、多数の小孔を有する液受け皿を設置し、
前記充填材の下端部が前記液受け皿に接し、あるいは、
隙間を有して設置される構造としたことを特徴とする充
填塔。
2. A plurality of packing materials are installed in multiple stages in the axial direction, and each packing material is constituted by a plurality of laminating materials having corrugated grooves arranged in parallel in a packed column, and adjacent laminating materials are A gas in which the corrugated grooves are arranged so as to intersect with each other, and the thin layered article has rows of small holes arranged at intervals so that the liquid flows down from the upper part and rises from the liquid and the lower part. In a packed column for gas-liquid contact for making a direct alternating current contact with each other, below the filler of the lowermost block of the filler composed of a plurality of blocks, a liquid tray having a large number of small holes is installed,
The lower end of the filling material contacts the liquid tray, or
A packed tower characterized by having a structure installed with a gap.
【請求項3】請求項1又は2記載の充填塔において、充
填塔が空気分離用の精留塔であることを特徴とする充填
塔。
3. The packed column according to claim 1, wherein the packed column is a rectification column for air separation.
JP19515294A 1994-08-19 1994-08-19 Packed column Pending JPH0857292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19515294A JPH0857292A (en) 1994-08-19 1994-08-19 Packed column

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19515294A JPH0857292A (en) 1994-08-19 1994-08-19 Packed column

Publications (1)

Publication Number Publication Date
JPH0857292A true JPH0857292A (en) 1996-03-05

Family

ID=16336301

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19515294A Pending JPH0857292A (en) 1994-08-19 1994-08-19 Packed column

Country Status (1)

Country Link
JP (1) JPH0857292A (en)

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