JPH11179101A - Internal heat exchange type distillation column and packing used therefor - Google Patents
Internal heat exchange type distillation column and packing used thereforInfo
- Publication number
- JPH11179101A JPH11179101A JP36493897A JP36493897A JPH11179101A JP H11179101 A JPH11179101 A JP H11179101A JP 36493897 A JP36493897 A JP 36493897A JP 36493897 A JP36493897 A JP 36493897A JP H11179101 A JPH11179101 A JP H11179101A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- tubes
- distillation column
- regions
- divided
- 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
- 238000012856 packing Methods 0.000 title claims abstract description 65
- 238000004821 distillation Methods 0.000 title claims abstract description 58
- 230000002093 peripheral effect Effects 0.000 claims abstract description 13
- 239000000945 filler Substances 0.000 claims description 65
- 239000000463 material Substances 0.000 claims description 46
- 238000011084 recovery Methods 0.000 claims description 24
- 239000007788 liquid Substances 0.000 abstract description 25
- 239000011800 void material Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 7
- 238000010030 laminating Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000007493 shaping process Methods 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 230000010354 integration Effects 0.000 description 2
- UNPLRYRWJLTVAE-UHFFFAOYSA-N Cloperastine hydrochloride Chemical compound Cl.C1=CC(Cl)=CC=C1C(C=1C=CC=CC=1)OCCN1CCCCC1 UNPLRYRWJLTVAE-UHFFFAOYSA-N 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本願発明は、低圧塔と高圧塔
を備え、高圧塔(濃縮部)側から、低圧塔(回収部)側
に熱移動させることにより両者の間で熱交換を行う内部
熱交換型の蒸留塔に関する。BACKGROUND OF THE INVENTION The present invention relates to an internal device comprising a low-pressure column and a high-pressure column, in which heat is transferred from a high-pressure column (concentrating section) to a low-pressure column (recovery section) to exchange heat between the two. The present invention relates to a heat exchange type distillation column.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】省エネ
ルギー性に優れた蒸留塔として、低圧塔と高圧塔とを備
え、両者の間で熱交換を行うように構成され、他との熱
の授受を必要としない内部熱交換型の蒸留塔が知られて
いる。この内部熱交換型蒸留塔は、蒸留操作の省エネル
ギー化を進める見地からすれば、究極の装置であること
は、原理的にも当然であり、また、学問上からも認めら
れているところである。2. Description of the Related Art As a distillation column excellent in energy saving, a low-pressure column and a high-pressure column are provided, and heat exchange is performed between the two columns. There is known an internal heat exchange type distillation column which does not require a heat exchanger. From the standpoint of promoting the energy saving of the distillation operation, this internal heat exchange type distillation column is naturally the ultimate device in principle, and it has been recognized from academia.
【0003】また、内部熱交換型蒸留塔として、複数管
を両端管板によって本体胴と連結させることにより、本
体胴の内部において、複数管の管内と管外が隔離された
構造とし、管内及び管外のそれぞれに気液の出入口を設
け、管内側と管外側の操作圧力に差をつけることにより
操作温度を異ならせ、複数管の管壁を伝熱面として、高
圧側から低圧側に熱移動させることにより、高圧側を濃
縮部、低圧側を回収部として一つの蒸留塔を構成するよ
うにした構造が提案されている(特許第2694425
号)。[0003] Further, as an internal heat exchange type distillation column, a plurality of tubes are connected to a main body by a tube plate at both ends, so that the inside and outside of the plurality of tubes are isolated inside the main body, and the inside and outside of the tubes are separated. Gas / liquid inlets and outlets are provided outside each pipe, and the operating temperature is made different by making the operating pressure different between the inside and outside of the pipe, and the heat is transferred from the high pressure side to the low pressure side using the pipe walls of multiple pipes as heat transfer surfaces. A structure has been proposed in which one distillation column is constituted by moving the high pressure side as a concentration section and the low pressure side as a recovery section (Japanese Patent No. 2694425).
issue).
【0004】そして、この内部熱交換型蒸留塔の型式と
しては、規則充填物を充填した充填塔型式を採用すると
ともに、管内側を低圧(回収部)側、管外側を高圧(濃
縮部)側とすることが有利である場合が多い。この充填
塔式蒸留塔において、塔(管)の充填物を充填した部分
(蒸留部)は、上から下に下降する下降液と、下から上
に上昇する上昇蒸気が接触して蒸留操作が行われる部分
であり、蒸留部においては水平断面の単位面積当たりの
下降液量が均一であることが望ましく、その場合に最も
高い蒸留分離効率が得られる。As the type of the internal heat exchange type distillation column, a packed column type packed with structured packing is adopted, and the inside of the tube is on the low pressure (recovery section) side, and the outside of the tube is on the high pressure (concentration section) side. Is often advantageous. In this packed column distillation column, the portion (distillation section) of the column (tube) filled with the packing is contacted with a descending liquid descending from top to bottom and a rising vapor rising from bottom to top, so that the distillation operation is performed. In the distillation section, it is desirable that the descending liquid amount per unit area of the horizontal section is uniform, and in this case, the highest distillation separation efficiency can be obtained.
【0005】ところで、濃縮部である管外側を充填塔と
する場合、 塔の平面断面形状内に充填物の充填されていない空隙
が存在しないこと、あるいは存在するとしても、平面断
面積に対する割合が無視小であるか、上昇蒸気の短絡
(チャンネリング)を防止する処理が施されているこ
と、 管外壁面上の下降液を充填物側に確実に戻す機能を有
していること(すなわち、管外側(濃縮部)では、上昇
蒸気が管外壁面上で凝縮して下降液となるため、下降液
が速やかに充填物側に移行して管外面が乾いているこ
と、あるいは管外面を下降している液量ができるだけ少
ないことが重要になる)の2つの要件を満たすことが必
要になる。[0005] By the way, when the outside of the tube, which is the enrichment section, is used as a packed tower, there is no void in which the packing is not filled in the planar sectional shape of the tower, or even if it is present, the ratio to the planar sectional area is small. Negligible, or have been treated to prevent short-circuiting (channeling) of rising steam, and have the function of reliably returning the descending liquid on the outer wall surface of the pipe to the packing side (ie, At the outside of the tube (concentration part), the rising vapor condenses on the outer wall of the tube to form a descending liquid, so the descending liquid quickly moves to the packing side and the outer surface of the tube is dry, or the outer surface of the tube descends. It is important that the amount of the liquid to be removed is as small as possible).
【0006】そして、上記の2つの要件を満たすための
方法として、例えば、板材に特殊加工により折り目をつ
けて所定の形状に成形した板製シートを複数枚積層した
板製充填物の周囲に、上部を外側に折り曲げ可能とした
カラー(バンド)を巻き付けた規則充填物(以下、単に
「充填物」ともいう)を挿入する方法がある。なお、カ
ラーの上部を外側に折り曲げ可能とする方法としては、
例えば、カラーの上部に、周方向に所定の間隔をおいて
複数の垂直の切り込みを入れる方法が考えられる。この
充填物を、カラーの上部が管(複数管)の外壁(管外
壁)に押し付けられるような状態で充填することができ
れば、管外壁上を流下する下降液を、カラーにより充填
物側に導いて、再び充填物上に分散させることが可能に
なる。As a method for satisfying the above two requirements, for example, a sheet material obtained by laminating a plurality of sheet sheets formed by folding a sheet material into a predetermined shape by performing a special process, There is a method of inserting a regular packing (hereinafter, also simply referred to as “filler”) around which a collar (band) whose upper part is bendable outward is wound. In addition, as a method to be able to bend the upper part of the collar outward,
For example, a method is conceivable in which a plurality of vertical cuts are formed at predetermined intervals in the circumferential direction at the top of the collar. If the filler can be filled in such a manner that the upper part of the collar is pressed against the outer wall (outer pipe wall) of the pipe (plural pipes), the descending liquid flowing down on the outer wall of the pipe is guided by the collar to the filler side. Thus, it can be dispersed again on the packing.
【0007】しかし、カラーを充填物の周囲に巻き付け
るためには、その部分が1個の充填物の外周面でなけれ
ば、実際に製作することができないという問題点があ
る。すなわち、これを管外側の形状に当てはめて考える
と、複数管の管外周をいずれかの位置で分割しないと管
外壁面に接する充填物面が1個の充填物の外周になり得
ないという問題点がある。However, in order to wind the collar around the filler, there is a problem that the collar cannot be actually manufactured unless the portion is the outer peripheral surface of one filler. That is, when this is applied to the outer shape of the pipe, the problem that the packing surface in contact with the outer wall of the pipe cannot become the outer circumference of one packing unless the outer circumference of the plurality of pipes is divided at any position. There is a point.
【0008】また、上記の2つの要件を満たすための別
の方法として、管外側に、管外壁に密着するように充填
物を配設し、管外壁を流下する下降液を効率よく充填物
側に戻す方法が考えられるが、本体胴の内部に複数管を
配設した塔の平面断面形状は、極めて複雑で、複数管の
管外壁に密着するように正確な寸法・形状を有する充填
物を製作すること、及びそれを複数管の管外壁に確実に
密着するように配設することは事実上困難であるのが実
情である。[0008] As another method for satisfying the above two requirements, a filler is disposed on the outside of the pipe so as to be in close contact with the outer wall of the pipe, and the descending liquid flowing down the outer wall of the pipe is efficiently discharged to the side of the filler. However, the plan sectional shape of the tower in which multiple pipes are arranged inside the main body is extremely complicated, and packing with accurate dimensions and shape is required to adhere to the outer wall of the multiple pipes. The fact is that it is practically difficult to manufacture and to arrange it in such a manner that it is in close contact with the outer wall of a plurality of tubes.
【0009】本願発明は、上記問題点を解決するもので
あり、濃縮部に大きな空隙が生じないように充填物が充
填されており、管外壁を流下する液量を適正量とするこ
とが可能で、効率よく内部熱交換蒸留を行うことが可能
な内部熱交換型蒸留塔、及びそれに用いられる、複数管
の管外壁に確実に密着するように充填することが可能な
充填物を提供することを目的とする。[0009] The present invention solves the above-mentioned problems, and the filling portion is filled so as not to generate a large void in the concentrating portion, and the amount of liquid flowing down the outer wall of the tube can be made an appropriate amount. To provide an internal heat exchange distillation column capable of efficiently performing internal heat exchange distillation, and a packing material used for the internal heat exchange distillation column, which can be packed so as to be surely adhered to the outer wall of a plurality of tubes. With the goal.
【0010】[0010]
【課題を解決するための手段】上記目的を達成するため
に、本願(請求項1)の内部熱交換型蒸留塔は、複数管
を両端管板によって本体胴と連結させることにより、本
体胴の内部において、複数管の管内と管外が隔離された
構造とし、管内及び管外のそれぞれに気液の出入口を設
け、管内側を低圧(回収部)側、管外側を高圧(濃縮
部)側として、操作圧力に差をつけることにより操作温
度を異ならせ、複数管の管壁を伝熱面として、高圧側の
管外(濃縮部)側から、低圧側の管内(回収部)側に熱
移動させることにより一つの蒸留塔を構成した内部熱交
換型蒸留塔であって、前記複数管の配列が三角配列であ
り、前記管外側の濃縮部が充填塔であって、平面的に見
た場合に中心を結ぶ線が略正三角形を形成する互いに隣
接する3本の管(3本管ユニット)の外周部と、前記略
正三角形を形成する線により区画される複数の領域(区
画領域)のそれぞれに、各区画領域に対応する平面形状
を有する充填物(分割充填物)が充填されていることを
特徴としている。In order to achieve the above object, the internal heat exchange type distillation column of the present invention (claim 1) has a structure in which a plurality of tubes are connected to the main body by means of a tube plate at both ends, whereby the main body is connected to the main body. Inside, the inside and outside of the pipes are separated from each other. Gas and liquid ports are provided inside and outside the pipe. The inside of the pipe is on the low pressure (recovery section) side, and the outside of the pipe is on the high pressure (concentration section) side. The operating temperature is varied by making the operating pressure different, and the heat is transferred from the outside of the high-pressure side pipe (concentration section) to the inside of the low-pressure side pipe (recovery section) using the pipe walls of multiple pipes as heat transfer surfaces. It is an internal heat exchange type distillation column which constitutes one distillation column by moving, the arrangement of the plurality of tubes is a triangular array, the enrichment section on the outside of the tube is a packed column, and viewed in plan. In this case, three tubes adjacent to each other (3) whose center connecting lines form a substantially equilateral triangle The outer periphery of the tube unit) and the plurality of regions (partitioned regions) defined by the lines forming the substantially equilateral triangle are each filled with a filler (split filler) having a planar shape corresponding to each of the divided regions. It is characterized by being.
【0011】3本管ユニットの外周部と、略正三角形を
形成する線により区画される複数の領域(区画領域)の
それぞれに、各区画領域に対応する平面形状を有する充
填物を充填するようにした場合、各区画領域の形状が同
一形状となるため、同一形状の一種類の充填物(分割充
填物)を用意するだけで、容易かつ確実に、管外壁と密
着するような態様で管外に充填物を充填することが可能
になる。[0011] An outer peripheral portion of the three-tube unit and a plurality of regions (partitioned regions) defined by lines forming a substantially equilateral triangle are each filled with a filler having a planar shape corresponding to each of the divided regions. In this case, since the shape of each partitioned area becomes the same, only one kind of packing (divided packing) of the same shape is prepared, and the pipe is easily and surely brought into close contact with the outer wall of the pipe. It becomes possible to fill the outside with a filler.
【0012】また、請求項2の内部熱交換型蒸留塔は、
複数管を両端管板によって本体胴と連結させることによ
り、本体胴の内部において、複数管の管内と管外が隔離
された構造とし、管内及び管外のそれぞれに気液の出入
口を設け、管内側を低圧(回収部)側、管外側を高圧
(濃縮部)側として、操作圧力に差をつけることにより
操作温度を異ならせ、複数管の管壁を伝熱面として、高
圧側の管外(濃縮部)側から、低圧側の管内(回収部)
側に熱移動させることにより一つの蒸留塔を構成した内
部熱交換型蒸留塔であって、前記複数管の配列が四角配
列であり、前記管外側の濃縮部が充填塔であって、平面
的に見た場合に中心を結ぶ線が略正方形を形成する互い
に対向・隣接する4本の管(4本管ユニット)の外周部
と、前記略正方形を形成する線により区画される複数の
領域(区画領域)のそれぞれに、各区画領域に対応する
平面形状を有する充填物(分割充填物)が充填されてい
ることを特徴としている。Further, the internal heat exchange type distillation column according to claim 2 is characterized in that:
By connecting the plurality of pipes to the main body by means of the pipe plates at both ends, the inside of the main body has a structure in which the inside and outside of the plurality of pipes are separated, and a gas-liquid inlet and outlet are provided inside and outside the pipe, respectively. The inside is on the low pressure (recovery section) side, and the outside of the pipe is on the high pressure (concentration section) side. The operating temperature is made different by differentiating the operating pressure. From the (concentration unit) side to the low pressure side tube (recovery unit)
An internal heat exchange type distillation column configured as one distillation column by heat transfer to the side, wherein the arrangement of the plurality of tubes is a square array, the enrichment section outside the tubes is a packed column, planar When viewed from above, the outer peripheral portions of four pipes (four-tube unit) facing and adjacent to each other, the lines connecting the centers forming a substantially square, and a plurality of regions ( Each of the divided regions is filled with a filler (split filler) having a planar shape corresponding to each of the divided regions.
【0013】前記4本管ユニットの外周部と、略正方形
を形成する線により区画される複数の領域(区画領域)
のそれぞれに、各区画領域に対応する平面形状を有する
充填物を充填するようにした場合にも、上記請求項1の
場合と同様に、各区画領域の形状が同一形状となるた
め、同一形状の一種類の充填物(分割充填物)を用意す
るだけで、容易かつ確実に、管外壁と密着するような態
様で管外に充填物を充填することが可能になる。An outer peripheral portion of the four-tube unit and a plurality of regions (partitioned regions) defined by lines forming a substantially square.
Is filled with a filler having a planar shape corresponding to each of the divided regions, the shape of each of the divided regions is the same as in the case of the above-mentioned claim 1, so that the same shape By simply preparing one type of packing (divided packing), it is possible to easily and reliably fill the outside of the tube with the packing so as to be in close contact with the outer wall of the tube.
【0014】また、請求項3の内部熱交換型蒸留塔は、
前記分割充填物の複数個が一体に形成された充填物ブロ
ックを複数個充填することにより、前記区画領域に充填
物が充填されていることを特徴としている。Further, the internal heat exchange type distillation column according to claim 3 comprises:
The divided region is filled with a filling material by filling a plurality of filling blocks in which a plurality of the divided filling materials are integrally formed.
【0015】分割充填物の複数個が一体に形成された充
填物ブロックを用いた場合、充填すべき充填物の個数が
減少するため、効率よく充填を行うことが可能になる。
なお、分割充填物の多数個を一体化してしまうと、かえ
って充填物ブロックの製造が複雑になったり、形状の異
なる複数の充填物を用意することが必要になったり、あ
るいは充填作業がかえって困難になったりする場合があ
るため、分割充填物をどの程度一体化するかは、複数管
の径や間隔など諸条件を考慮して定めることが好まし
い。When a packing block in which a plurality of divided packings are integrally formed is used, the number of packings to be filled is reduced, so that packing can be performed efficiently.
In addition, if a large number of divided packings are integrated, the manufacture of the packing block becomes complicated on the contrary, it is necessary to prepare a plurality of packings having different shapes, or the filling work is rather difficult Therefore, it is preferable that the degree of integration of the divided packing materials is determined in consideration of various conditions such as the diameters and intervals of the plurality of pipes.
【0016】また、請求項4の内部熱交換型蒸留塔は、
本体胴内壁と、複数管の本体胴に対向する部分の間に形
成される空隙には、前記充填物(分割充填物)以外の充
填物が充填されていることを特徴としている。The internal heat exchange type distillation column according to claim 4 is characterized in that:
A gap formed between the inner wall of the main body and the portion of the plurality of tubes facing the main body is filled with a filler other than the filler (divided filler).
【0017】本体胴内壁と、複数管の本体胴に対向する
部分の間に形成される空隙には、分割充填物以外の、空
隙の形状に適した充填物を充填することにより、本体胴
内の管外全体に、効率よく充填物を充填することが可能
になり、本願発明をより実効あらしめることができる。The space formed between the inner wall of the main body and the portion of the plurality of pipes facing the main body is filled with a filling material other than the divided filling material, which is suitable for the shape of the space. , It is possible to efficiently fill the entire outside of the tube with the filler, and the present invention can be made more effective.
【0018】また、本願(請求項5)の充填物は、三角
配列の複数管を両端管板によって本体胴と連結させるこ
とにより、複数管の管内と管外が隔離された構造とした
塔(本体胴)内の、複数管の管外に充填物を充填する場
合に用いられる充填物であって、平面的に見た場合に中
心を結ぶ線が略正三角形を形成する互いに隣接する3本
の管(三本管ユニット)の外周部と、前記略正三角形を
形成する線により区画される複数の領域(区画領域)に
対応する平面形状、又は、前記区画領域を複数個接続し
た平面形状を有するように分割形成されていることを特
徴としている。The packing of the present invention (claim 5) has a structure in which a plurality of tubes in a triangular arrangement are connected to the main body by means of a tube plate at both ends so that the inside and outside of the plurality of tubes are isolated. A filling material used when filling the filling material outside the plurality of tubes in the main body, three lines adjacent to each other, the lines connecting the centers form a substantially equilateral triangle when viewed in a plan view A planar shape corresponding to the outer peripheral portion of the pipe (three-tube unit) and a plurality of regions (partitioned regions) defined by lines forming the substantially equilateral triangle, or a planar shape in which a plurality of the divided regions are connected Is formed so as to have the following.
【0019】この充填物は、平面的に見た場合に中心を
結ぶ線が略正三角形を形成する互いに隣接する3本の管
(3本管ユニット)の外周部と、前記略正三角形を形成
する線により区画される複数の領域(区画領域)に対応
する平面形状を有するように分割形成されているため、
同一種類の充填物を所定個数用意するだけで、容易かつ
確実に、管外壁と密着するような態様で管外に充填物が
充填された内部熱交換型蒸留塔を構成することが可能に
なる。また、充填物が、区画領域を複数個接続した平面
形状を有するようにした場合、充填すべき充填物の個数
を減らして、効率よく充填を行うことが可能になる。な
お、分割充填物をあまり多く一体化してしまうと、かえ
って充填物ブロックの製造が複雑になったり、形状の異
なる複数の充填物を用意することが必要になったり、あ
るいは充填作業がかえって困難になったりする場合があ
るため、分割充填物をどの程度一体化するかは、複数管
の径や間隔などを考慮して定めることが好ましいこと
は、上述の請求項3の場合と同様である。The packing has the outer peripheral portions of three adjacent pipes (three-tube unit) whose lines connecting the centers form a substantially equilateral triangle when viewed in a plan view, and the above-described substantially equilateral triangle. Is divided and formed so as to have a planar shape corresponding to a plurality of regions (partitioned regions) partitioned by a line.
By simply preparing a predetermined number of the same type of packing, it is possible to easily and reliably configure an internal heat exchange distillation column in which the packing is filled outside the tube in such a manner as to be in close contact with the outer wall of the tube. . Further, when the filler has a planar shape in which a plurality of partitioned areas are connected, the number of fillers to be filled can be reduced, and efficient filling can be performed. In addition, if too many divided packings are integrated, the manufacture of the packing block becomes rather complicated, or it becomes necessary to prepare a plurality of packings having different shapes, or the filling work becomes rather difficult. In some cases, the degree of integration of the divided packing materials is preferably determined in consideration of the diameters, intervals, and the like of the plurality of pipes, as in the case of claim 3 described above.
【0020】また、本願(請求項6)の充填物は、四角
配列の複数管を両端管板によって本体胴と連結させるこ
とにより、複数管の管内と管外が隔離された構造とした
塔(本体胴)内の、複数管の管外に充填物を充填する場
合に用いられる充填物であって、平面的に見た場合に中
心を結ぶ線が略正方形を形成する互いに対向・隣接する
4本の管(4本管ユニット)の外周部と、前記略正方形
を形成する線により区画される複数の領域(区画領域)
に対応する平面形状、又は、前記区画領域を複数個接続
した平面形状を有するように分割形成されていることを
特徴としている。The packing of the present invention (Claim 6) has a structure in which the inside and outside of the plurality of tubes are isolated by connecting a plurality of tubes in a square array to the main body by means of a tube plate at both ends. A filling material used to fill the outside of a plurality of pipes in the main body), wherein lines connecting the centers form a substantially square shape when viewed in a plan view, and are opposed to and adjacent to each other. A plurality of regions (partitioned regions) divided by the outer peripheral portion of a main tube (four-tube unit) and the line forming the substantially square
Or a divided shape having a planar shape corresponding to a plurality of the divided regions.
【0021】この充填物は、平面的に見た場合に中心を
結ぶ線が略正方形を形成する互いに対向・隣接する4本
の管(4本管ユニット)の外周部と、略正方形を形成す
る線により区画される複数の領域(区画領域)に対応す
る平面形状を有するように分割形成されているため、同
一種類の充填物を所定個数用意するだけで、容易かつ確
実に、管外壁と密着するような態様で管外に充填物が充
填された内部熱交換型蒸留塔を構成することが可能にな
る。また、充填物が、区画領域を複数個接続した平面形
状を有するようにした場合、充填すべき充填物の個数を
減らして、効率よく充填を行うことが可能になる。This packing forms a substantially square shape with the outer peripheral portions of four tubes (four-tube unit) opposed to each other and adjacent to each other, the lines connecting the centers when viewed in a plan view form a substantially square shape. Since it is divided and formed so as to have a planar shape corresponding to a plurality of regions (partitioned regions) partitioned by lines, it is easy and sure to adhere to the outer wall of the pipe simply by preparing a predetermined number of the same type of filler. In this manner, it is possible to configure an internal heat exchange type distillation column in which the packing is filled outside the tube. Further, when the filler has a planar shape in which a plurality of partitioned areas are connected, the number of fillers to be filled can be reduced, and efficient filling can be performed.
【0022】[0022]
【発明の実施の形態】以下、この発明の実施の形態を示
して、その特徴とするところを更に詳しく説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described, and features thereof will be described in more detail.
【0023】[実施形態1]図2は本願発明の一実施例
にかかる内部熱交換型蒸留塔の概略構成を示す正面断面
図である。[Embodiment 1] FIG. 2 is a front sectional view showing a schematic configuration of an internal heat exchange type distillation column according to one embodiment of the present invention.
【0024】この内部熱交換型蒸留塔(を構成する構造
体)は、本体胴1と、本体胴1内に挿入された複数管2
5を両端管板(上側管板3a及び下側管板3b)によっ
て本体胴1と連結させることにより形成されており、複
数管25の管内(回収部)4と管外(濃縮部)5が隔離
された構造を有している。そして、管外(濃縮部)には
規則充填物が充填されており、管内(回収部)4にも規
則充填物が充填されている。The internal heat exchange type distillation column (structure constituting it) includes a main body 1 and a plurality of tubes 2 inserted into the main body 1.
5 is formed by connecting the main body 1 with both end tube sheets (upper tube sheet 3a and lower tube sheet 3b), and the inside (collection unit) 4 and the outside tube (concentration unit) 5 of the plurality of tubes 25 are formed. It has an isolated structure. The outside of the tube (concentrating unit) is filled with the ordered packing, and the inside of the tube (recovering unit) 4 is also filled with the ordered packing.
【0025】また、本体胴1の上部には、管外(濃縮
部)5に液を供給するための濃縮部液入口6、管外(濃
縮部)5からの蒸気を抜き出す濃縮部蒸気出口7が配設
されており、上側管板3aより上側の、管内(回収部)
4と連通する端室14aには、管内(回収部)4に液を
供給するための回収部液入口8が配設され、また、管内
(回収部)4からの蒸気を抜き出す回収部蒸気出口9が
配設されている。In the upper part of the main body 1, a liquid inlet 6 for supplying a liquid to the outside of the tube (concentration unit) 5, and a vapor outlet 7 for the condensation unit for extracting vapor from the outside of the tube (concentration unit) 5. Is disposed inside the pipe (recovery section) above the upper pipe sheet 3a.
A recovery section liquid inlet 8 for supplying liquid to the inside of the pipe (recovery section) 4 is provided in the end chamber 14 a communicating with the pipe 4, and a recovery section steam outlet for extracting vapor from the inside of the pipe (collection section) 4. 9 are provided.
【0026】一方、本体胴1の下部には、管外(濃縮
部)5に蒸気を供給するための濃縮部蒸気入口10、管
外(濃縮部)5からの液を抜き出す濃縮部液出口11が
配設されており、下側管板3bより下側の、管内(回収
部)4と連通する端室14bには、管内(回収部)4に
蒸気を供給するための回収部蒸気入口12が配設され、
また、管内(回収部)4からの液を抜き出す回収部液出
口13が配設されている。On the other hand, in the lower part of the main body 1, a vapor inlet 10 for supplying the vapor to the outside (concentrating unit) 5 of the tube, and a liquid outlet 11 for the condensing unit for extracting the liquid from the outside (concentrating unit) 5. A recovery section steam inlet 12 for supplying steam to the inside of the pipe (recovery section) 4 is provided in an end chamber 14b below the lower tube sheet 3b and communicating with the inside of the pipe (recovery section) 4. Is arranged,
In addition, a recovery section liquid outlet 13 for extracting the liquid from the inside of the pipe (recovery section) 4 is provided.
【0027】この実施形態1の内部熱交換型蒸留塔にお
いては、複数管25は、図1に示すように、三角配列と
なっており、平面的に見た場合に、互いに隣接する3本
の管25(25a,25b,25c)(3本管ユニット
U1)の中心A,B,Cを結ぶ線X,Y,Zが正三角形
27を形成するように配列されている。In the internal heat exchange type distillation column of the first embodiment, the plurality of tubes 25 are arranged in a triangular arrangement as shown in FIG. Lines X, Y, and Z connecting the centers A, B, and C of the tubes 25 (25a, 25b, 25c) (three-tube unit U1) are arranged to form an equilateral triangle 27.
【0028】そして、この内部熱交換型蒸留塔において
は、3本管ユニットU1を構成する各管25a,25
b,25cの外周部と、上記正三角形27を形成する線
X,Y,Zにより区画される複数の領域(区画領域)S
1のそれぞれに、各区画領域S1に対応する平面形状を
有する充填物(分割充填物)31,31……が充填され
ている(すなわち、図1の太線L1で囲まれた範囲内の
区画領域S1(ハッチングを付した部分)には分割充填
物31が充填されている)。なお、分轄充填物31とし
ては、板材に特殊加工により折り目をつけて所定の形状
に成形した板製シートを複数枚積層してなる板製充填物
(規則充填物)を用いた。但し、分割充填物31は、こ
れに限らず、網材を所定の形状に成形した網製充填物そ
の他の種々のタイプの充填物を用いることが可能であ
る。Then, in this internal heat exchange type distillation column, each of the tubes 25a, 25 constituting the three-tube unit U1.
b, 25c and a plurality of regions (partitioned regions) S defined by lines X, Y, Z forming the equilateral triangle 27
1 are filled with fillers (divided fillers) 31, 31,... Having a planar shape corresponding to each of the divided areas S1 (that is, the divided areas within the range surrounded by the thick line L1 in FIG. 1). S1 (hatched portion) is filled with the divided filler 31). In addition, as the divided filling material 31, a plate-like filling material (ordered filling material) obtained by laminating a plurality of plate-like sheets formed by folding a plate material into a predetermined shape by special processing was used. However, the divided filling material 31 is not limited to this, and it is possible to use a filling material made of a net obtained by shaping a net material into a predetermined shape and other various types of filling materials.
【0029】また、本体胴1の内壁1aと、複数管25
の本体胴1に対向する部分の間に形成される空隙29に
は、分割充填物31とは異なる、空隙29の形状に対応
する充填物32が充填されている。なお、この充填物3
2の、本体胴1の内壁1aと複数管25の管外壁26と
対向する部分にはカラーを設けることが望ましいが、充
填物32を分割形成することにより、カラーを設けるべ
き部分が充填物の外周面となるため、カラーを容易に取
り付けることができる。なお、この実施形態1では、充
填物32として、板材に特殊加工により折り目をつけて
所定の形状に成形した板製シートを複数枚積層してなる
板製充填物(規則充填物)を用いたが、充填物32とし
ては、これに限らず、網材を所定の形状に成形した網製
充填物その他の種々のタイプの充填物を用いることが可
能である。Also, the inner wall 1a of the main body 1 and a plurality of tubes 25
The space 29 formed between the portions facing the main body 1 is filled with a filler 32 different from the divided filler 31 and corresponding to the shape of the space 29. In addition, this filling 3
It is desirable to provide a collar on the portion of the body 2 facing the inner wall 1a of the main body 1 and the outer wall 26 of the plurality of tubes 25. However, by forming the filler 32 separately, the portion where the collar is to be provided is filled with the filler. Since the outer peripheral surface is provided, the collar can be easily attached. In the first embodiment, as the filler 32, a plate-like filler (ordered filler) obtained by laminating a plurality of plate-like sheets formed by folding a plate material into a predetermined shape by special processing is used. However, the filler 32 is not limited to this, and a mesh filler formed by shaping a net material into a predetermined shape and other various types of fillers can be used.
【0030】この実施形態1の内部熱交換型蒸留塔にお
いては、上述のように、同一平面形状の各区画領域S1
に分割充填物31を充填するようにしているので、同一
形状の一種類の充填物(分割充填物)を用意するだけ
で、容易かつ確実に、複数管25の管外壁26と密着す
るような態様で管外5に充填物を充填することが可能に
なる。また、本体胴1の内壁1aと、複数管25の本体
胴1に対向する部分の間に形成される空隙29には、分
割充填物31とは異なる、空隙29の形状に対応する充
填物32を充填するようにしており、この充填物32に
は、カラーを設けることが可能であるため、本体胴1の
内壁1aと、複数管25の本体胴1に対向する部分の間
に形成される空隙29を確実に埋めることが可能にな
る。In the internal heat exchange type distillation column according to the first embodiment, as described above, each divided area S1 having the same planar shape is used.
Since the divided filling material 31 is filled with a single filling material of the same shape (divided filling material), it is possible to easily and surely adhere to the outer wall 26 of the plurality of tubes 25 simply by preparing the same kind of filling material (divided filling material). In this manner, the outer tube 5 can be filled with the filler. A gap 29 formed between the inner wall 1a of the main body 1 and a portion of the plurality of tubes 25 facing the main body 1 has a filling 32 corresponding to the shape of the gap 29, which is different from the divided filling 31. Since the filler 32 can be provided with a collar, it is formed between the inner wall 1a of the main body 1 and the portion of the plurality of tubes 25 facing the main body 1. The gap 29 can be reliably filled.
【0031】なお、この実施形態1では、区画領域S1
に対応する平面形状を有する分轄充填物31を用いた場
合について説明したが、区画領域S1を複数個接続した
平面形状を有する充填物ブロックを用いることも可能で
あり、その場合には、充填すべき充填物の個数を減らし
て、効率よく充填を行うことが可能になる。In the first embodiment, the divided area S1
Although the case where the divided filling material 31 having the planar shape corresponding to the above is used has been described, it is also possible to use a filling block having a planar shape in which a plurality of the divided areas S1 are connected. It is possible to reduce the number of fillers to be filled and to perform efficient filling.
【0032】[実施形態2]図3は、本願発明の他の実
施形態にかかる内部熱交換型蒸留塔の要部(濃縮部な
ど)の構成を示す平面断面図である。この実施形態2の
内部熱交換型蒸留塔においては、複数管25は、図3に
示すように、四角配列となっており、平面的に見た場合
に、互いに隣接する4本の管25(25a,25b,2
5c,25d)(4本管ユニットU2)の中心A,B,
C,Dを結ぶ線W,X,Y,Zが正方形28を形成する
ように配列されている。[Embodiment 2] FIG. 3 is a cross-sectional plan view showing the configuration of a main part (such as a concentrator) of an internal heat exchange type distillation column according to another embodiment of the present invention. In the internal heat exchange type distillation column according to the second embodiment, the plurality of tubes 25 are arranged in a square as shown in FIG. 3, and four tubes 25 ( 25a, 25b, 2
5c, 25d) The centers A, B,
Lines W, X, Y, and Z connecting C and D are arranged to form a square 28.
【0033】そして、この内部熱交換型蒸留塔において
は、4本管ユニットU2を構成する各管25a,25
b,25c,25dの外周部と、上記正方形28を形成
する線W,X,Y,Zにより区画される複数の領域(区
画領域)S2のそれぞれに、各区画領域S2に対応する
平面形状を有する充填物(分割充填物)41,41……
が充填されている(すなわち、図3の太線L2で囲まれ
た範囲内の区画領域S2(ハッチングを付した部分)に
は分割充填物41が充填されている)。なお、分轄充填
物41としては、板材に特殊加工により折り目をつけて
所定の形状に成形した板製シートを複数枚積層してなる
板製充填物(規則充填物)を用いた。但し、分割充填物
41は、これに限らず、網材を所定の形状に成形した網
製充填物その他の種々のタイプの充填物を用いることが
可能である。In this internal heat exchange type distillation column, each of the tubes 25a, 25 constituting the four-tube unit U2
b, 25c, and 25d, and a plurality of regions (partitioned regions) S2 defined by the lines W, X, Y, and Z that form the square 28, each having a planar shape corresponding to each of the divided regions S2. Filling (split filling) 41, 41 ...
(That is, the divided area 41 is filled in the partitioned area S2 (hatched portion) in the area surrounded by the thick line L2 in FIG. 3). In addition, as the divided charge 41, a plate-like filler (ordered filler) formed by laminating a plurality of plate-like sheets formed by folding a plate material into a predetermined shape by special processing was used. However, the divided filler 41 is not limited to this, and various types of filler such as a net filler obtained by molding a net material into a predetermined shape can be used.
【0034】また、本体胴1の内壁1aと、複数管25
の本体胴1に対向する部分の間に形成される空隙30に
は、分割充填物41とは異なる、空隙30の形状に対応
する充填物42が充填されている。なお、この実施形態
2では、充填物42として、板材に特殊加工により折り
目をつけて所定の形状に成形した板製シートを複数枚積
層してなる板製充填物(規則充填物)を用いた。但し、
充填物42としては、これに限らず、網材を所定の形状
に成形した網製充填物その他の種々のタイプの充填物を
用いることが可能である。なお、この充填物42も、分
割形成することによりカラーを容易に取り付けることが
可能である。The inner wall 1a of the main body 1 and a plurality of tubes 25
The gap 30 formed between the portions facing the main body 1 is filled with a filling material 42 that is different from the divided filling material 41 and corresponds to the shape of the gap 30. In the second embodiment, as the filler 42, a plate-like filler (ordered filler) formed by laminating a plurality of plate-like sheets formed by folding a plate material into a predetermined shape by special processing is used. . However,
The filler 42 is not limited to this, and various types of fillers, such as a net-like filler formed by shaping a net material into a predetermined shape, can be used. The filler 42 can also be easily attached with a collar by being formed separately.
【0035】この実施形態2の内部熱交換型蒸留塔にお
いても、上述の実施形態1の場合と同様に、分割充填物
41を用いるようにしているので、同一形状の一種類の
充填物(分割充填物)41を用意するだけで、容易かつ
確実に、複数管25の管外壁26と密着するような態様
で管外5に充填物を充填することが可能になる。また、
本体胴1の内壁1aと、複数管25の本体胴1に対向す
る部分の間に形成される空隙30には、分割充填物41
とは異なる、空隙30の形状に対応する充填物42を充
填するようにしており、この充填物42は、分割形成す
ることによりに容易にカラーを設けることが可能である
ため、本体胴1の内壁1aと、複数管25の本体胴1に
対向する部分の間に形成される空隙30を確実に埋める
ことができる。In the internal heat exchange type distillation column according to the second embodiment, as in the case of the above-described first embodiment, the divided packing 41 is used. Only by preparing the filling material 41, it is possible to easily and surely fill the outer tube 5 with the filling material in such a manner as to be in close contact with the outer tube wall 26 of the plurality of tubes 25. Also,
In the gap 30 formed between the inner wall 1a of the main body 1 and the portion of the plurality of pipes 25 facing the main body 1, divided fillings 41 are provided.
The filling material 42 corresponding to the shape of the cavity 30 is filled with the filling material 42. Since the filling material 42 can be easily provided with a collar by being divided and formed, the filling material 42 of the main body 1 is formed. The space 30 formed between the inner wall 1a and the portion of the plurality of tubes 25 facing the main body 1 can be reliably filled.
【0036】なお、この実施形態2においても、区画領
域S2に対応する平面形状を有する分轄充填物41を用
いた場合について説明したが、区画領域S2を複数個接
続した平面形状を有する充填物ブロックを用いることも
可能であり、その場合、充填すべき充填物の個数を減ら
して、効率よく充填を行うことが可能になる。In the second embodiment, the case where the divided filling material 41 having the planar shape corresponding to the partitioned area S2 is used is described. However, the filler block having the planar shape in which a plurality of the partitioned areas S2 are connected is described. Can be used, and in that case, the number of fillers to be filled can be reduced and the filling can be performed efficiently.
【0037】なお、本願発明は、上記実施形態1,2に
限定されるものではなく、複数管の具体的な配設位置や
配設本数、区画領域の具体的形状などに関し、発明の要
旨の範囲内において、種々の応用、変形を加えることが
可能である。また、本願においては、複数管の配列態様
が三角配列及び四角配列である場合を主にして説明した
が、他の方式により、一定の規則性を持って複数管を配
列する場合にも、本願発明を適用することが可能であ
る。The present invention is not limited to the first and second embodiments, but relates to the specific arrangement position and the number of the plural pipes, the specific shape of the divided area, and the like. Various applications and modifications can be made within the scope. In the present application, the case where the arrangement of the plurality of tubes is a triangular arrangement and a square arrangement has been mainly described. However, the present invention is also applicable to the case where the plurality of tubes are arranged with a certain regularity by another method. The invention can be applied.
【0038】[0038]
【発明の効果】上述のように、本願発明(請求項1)の
内部熱交換型蒸留塔は、3本管ユニットの外周部と、略
正三角形を形成する線により区画される複数の領域(区
画領域)のそれぞれに、各区画領域に対応する平面形状
を有する充填物を充填するようにしており、各区画領域
の形状が同一形状となるため、同一形状の一種類の充填
物(分割充填物)を用意するだけで、容易かつ確実に、
管外壁と密着するような態様で管外に充填物を充填する
ことが可能で、効率よく内部熱交換蒸留を行うことが可
能になる。As described above, the internal heat exchange type distillation column of the present invention (claim 1) has an outer peripheral portion of a three-tube unit and a plurality of regions (parts) defined by lines forming a substantially equilateral triangle. Each of the divided areas is filled with a filler having a planar shape corresponding to each of the divided areas. Since each of the divided areas has the same shape, one type of the same shaped filler (divided filling) is used. Object), easily and reliably,
The packing can be filled outside the tube in such a manner as to be in close contact with the outer wall of the tube, and the internal heat exchange distillation can be performed efficiently.
【0039】また、請求項2の内部熱交換型蒸留塔は、
4本管ユニットの外周部と、略正方形を形成する線によ
り区画される複数の領域(区画領域)のそれぞれに、各
区画領域に対応する平面形状を有する充填物を充填する
ようにしているので、上記の請求項1の内部熱交換型蒸
留塔の場合と同様に、各区画領域の形状が同一形状とな
り、同一形状の一種類の充填物(分割充填物)を用意す
るだけで、容易かつ確実に、管外壁と密着するような態
様で管外に充填物を充填することが可能で、効率よく内
部熱交換蒸留を行うことが可能になる。Further, the internal heat exchange type distillation column according to claim 2 is:
Since the outer periphery of the four-tube unit and a plurality of regions (partitioned regions) defined by lines forming a substantially square are filled with a filler having a planar shape corresponding to each of the divided regions. As in the case of the internal heat exchange type distillation column according to the first aspect, the shape of each partitioned area becomes the same, and it is easy and easy to prepare one type of packing (divided packing) having the same shape. It is possible to reliably fill the outside of the tube with the packing so as to be in close contact with the outside wall of the tube, and it is possible to efficiently perform the internal heat exchange distillation.
【0040】また、請求項3の内部熱交換型蒸留塔のよ
うに、分割充填物の複数個が一体に形成された充填物ブ
ロックを用いた場合、充填すべき充填物の個数が減少す
るため、効率よく充填を行うことが可能になる。Further, when a packing block in which a plurality of divided packings are integrally formed is used as in the internal heat exchange type distillation column according to claim 3, the number of packings to be packed is reduced. It is possible to perform the filling efficiently.
【0041】また、請求項4の内部熱交換型蒸留塔のよ
うに、本体胴内壁と、複数管の本体胴に対向する部分の
間に形成される空隙には、分割充填物以外の、空隙の形
状に適した充填物を充填するようにした場合、本体胴内
の管外全体に、効率よく充填物を充填することが可能に
なり、本願発明をより実効あらしめることができる。Further, as in the internal heat exchange type distillation column according to the fourth aspect, the space formed between the inner wall of the main body and the portion of the plurality of tubes facing the main body is formed by a space other than the divided packing. When the filling material suitable for the shape is filled, it is possible to efficiently fill the entire outside of the tube inside the main body with the filling material, so that the present invention can be made more effective.
【0042】また、本願(請求項5)の充填物は、平面
的に見た場合に中心を結ぶ線が略正三角形を形成する互
いに隣接する3本の管(3本管ユニット)の外周部と、
前記略正三角形を形成する線により区画される複数の領
域(区画領域)に対応する平面形状を有するように分割
形成されているため、同一種類の充填物を所定個数用意
するだけで、容易かつ確実に、管外壁と密着するような
態様で管外に充填物が充填された内部熱交換型蒸留塔を
構成することが可能になる。また、充填物が、区画領域
を複数個接続した平面形状を有するようにした場合、充
填すべき充填物の個数を減らして、効率よく充填を行う
ことが可能になる。The packing according to the present invention (claim 5) has an outer peripheral portion of three adjacent pipes (three-tube unit) whose lines connecting the centers form a substantially equilateral triangle when viewed in a plan view. When,
Since it is divided and formed so as to have a planar shape corresponding to a plurality of regions (partitioned regions) defined by lines forming the substantially equilateral triangle, it is easy and simple to prepare a predetermined number of the same type of filler. It is possible to form the internal heat exchange type distillation column in which the packing is filled outside the tube in such a manner as to be in close contact with the outer wall of the tube. Further, when the filler has a planar shape in which a plurality of partitioned areas are connected, the number of fillers to be filled can be reduced, and efficient filling can be performed.
【0043】また、本願(請求項6)の充填物は、平面
的に見た場合に中心を結ぶ線が略正方形を形成する互い
に対向・隣接する4本の管(4本管ユニット)の外周部
と、略正方形を形成する線により区画される複数の領域
(区画領域)に対応する平面形状を有するように分割形
成されているため、同一種類の充填物を所定個数用意す
るだけで、容易かつ確実に、管外壁と密着するような態
様で管外に充填物が充填された内部熱交換型蒸留塔を構
成することが可能になる。また、充填物が、区画領域を
複数個接続した平面形状を有するようにした場合、充填
すべき充填物の個数を減らして、効率よく充填を行うこ
とが可能になる。The packing according to the present invention (claim 6) has an outer periphery of four pipes (four pipe units) facing and adjacent to each other, the lines connecting the centers forming a substantially square shape when viewed in a plan view. It is divided and formed so as to have a planar shape corresponding to a portion and a plurality of regions (partitioned regions) defined by lines forming a substantially square, so that it is easy to prepare only a predetermined number of the same type of filler. In addition, it is possible to form the internal heat exchange type distillation column in which the packing is filled outside the tube in such a manner as to be in close contact with the outer wall of the tube. Further, when the filler has a planar shape in which a plurality of partitioned areas are connected, the number of fillers to be filled can be reduced, and efficient filling can be performed.
【図1】本願発明の一実施形態にかかる内部熱交換型蒸
留塔の要部(濃縮部など)の構成を示す平面断面図であ
る。FIG. 1 is a plan cross-sectional view showing a configuration of a main part (such as a concentration part) of an internal heat exchange type distillation column according to an embodiment of the present invention.
【図2】本願発明の一実施例にかかる内部熱交換型蒸留
塔を示す正面断面図である。FIG. 2 is a front sectional view showing an internal heat exchange type distillation column according to one embodiment of the present invention.
【図3】本願発明の他の実施形態にかかる内部熱交換型
蒸留塔の要部(濃縮部など)の構成を示す平面断面図で
ある。FIG. 3 is a cross-sectional plan view showing a configuration of a main part (such as a concentration part) of an internal heat exchange type distillation column according to another embodiment of the present invention.
1 本体胴 1a 本体胴の内壁 3a 上側管板 3b 下側管板 4 管内(回収部) 5 管外(濃縮部) 6 濃縮部液入口 7 濃縮部蒸気出口 8 回収部液入口 9 回収部蒸気出口 10 濃縮部蒸気入口 11 濃縮部液出口 12 回収部蒸気入口 13 回収部液出口 14a,14b 端室 25,25a,25b,25c,25d 管(複数
管) 26 管外壁 27 正三角形 28 正方形 29,30 空隙 31,41 分割充填物 32,42 充填物 S1,S2 区画領域 U1 3本管ユニット U2 4本管ユニット A,B,C,D 管の中心 W,X,Y,Z 線DESCRIPTION OF SYMBOLS 1 Main body 1a Inner wall of main body 3a Upper tube sheet 3b Lower tube sheet 4 Inside pipe (recovery section) 5 Outside pipe (concentration section) 6 Concentration section liquid inlet 7 Concentration section vapor outlet 8 Recovery section liquid inlet 9 Recovery section vapor outlet DESCRIPTION OF SYMBOLS 10 Concentration part vapor inlet 11 Concentration part liquid outlet 12 Recovery part vapor inlet 13 Collection part liquid outlet 14a, 14b End chamber 25, 25a, 25b, 25c, 25d Tube (multiple tubes) 26 Tube outer wall 27 Regular triangle 28 Square 29, 30 Voids 31, 41 Divided packing 32, 42 Filling S1, S2 Partitioned area U1 Three pipe unit U2 Four pipe unit A, B, C, D Center of pipe W, X, Y, Z line
フロントページの続き (72)発明者 中西 俊成 兵庫県尼崎市杭瀬寺島2丁目1番2号 木 村化工機株式会社内 (72)発明者 野田 秀夫 兵庫県尼崎市南七松町2丁目9番7号 関 西化学機械製作株式會社内 (72)発明者 前田 ▲泰▼ 東京都中央区八丁堀二丁目25番10号 丸善 石油化学株式会社内Continuing from the front page (72) Inventor Toshinari Nakanishi 2-1-2-2, Kuise-Terashima, Amagasaki City, Hyogo Prefecture Inside Kimura Kakoki Co., Ltd. (72) Inventor Hideo Noda 2-97-7 Minami-Nanamatsucho, Amagasaki City, Hyogo Prefecture Seki In-house of Nishi Chemical Machinery Co., Ltd. (72) Inventor ▲ Yasu ▼ 2-25-10 Hatchobori, Chuo-ku, Tokyo
Claims (6)
せることにより、本体胴の内部において、複数管の管内
と管外が隔離された構造とし、管内及び管外のそれぞれ
に気液の出入口を設け、管内側を低圧(回収部)側、管
外側を高圧(濃縮部)側として、操作圧力に差をつける
ことにより操作温度を異ならせ、複数管の管壁を伝熱面
として、高圧側の管外(濃縮部)側から、低圧側の管内
(回収部)側に熱移動させることにより一つの蒸留塔を
構成した内部熱交換型蒸留塔であって、 前記複数管の配列が三角配列であり、 前記管外側の濃縮部が充填塔であって、平面的に見た場
合に中心を結ぶ線が略正三角形を形成する互いに隣接す
る3本の管(3本管ユニット)の外周部と、前記略正三
角形を形成する線により区画される複数の領域(区画領
域)のそれぞれに、各区画領域に対応する平面形状を有
する充填物(分割充填物)が充填されていることを特徴
とする内部熱交換型蒸留塔。1. A structure in which a plurality of pipes are connected to a main body by means of a tube plate at both ends, so that the inside and the outside of the plurality of pipes are separated from each other inside the main body. An inlet / outlet is provided, the inside of the pipe is set to the low pressure (recovery section) side, and the outside of the pipe is set to the high pressure (concentration section) side. An internal heat exchange type distillation column in which one distillation column is constituted by transferring heat from the outside of the high pressure side tube (concentration section) to the inside of the low pressure side pipe (recovery section) side. A triangular arrangement, wherein the enrichment section on the outer side of the tubes is a packed tower, and a line connecting the centers in a plan view forms three substantially adjacent triangles (three-tube unit). An outer peripheral portion and a plurality of regions ( In each of the image areas), the internal heat exchanging type distillation column packing (split packing) is characterized in that it is filled with a planar shape corresponding to the partitioned regions.
せることにより、本体胴の内部において、複数管の管内
と管外が隔離された構造とし、管内及び管外のそれぞれ
に気液の出入口を設け、管内側を低圧(回収部)側、管
外側を高圧(濃縮部)側として、操作圧力に差をつける
ことにより操作温度を異ならせ、複数管の管壁を伝熱面
として、高圧側の管外(濃縮部)側から、低圧側の管内
(回収部)側に熱移動させることにより一つの蒸留塔を
構成した内部熱交換型蒸留塔であって、 前記複数管の配列が四角配列であり、 前記管外側の濃縮部が充填塔であって、平面的に見た場
合に中心を結ぶ線が略正方形を形成する互いに対向・隣
接する4本の管(4本管ユニット)の外周部と、前記略
正方形を形成する線により区画される複数の領域(区画
領域)のそれぞれに、各区画領域に対応する平面形状を
有する充填物(分割充填物)が充填されていることを特
徴とする内部熱交換型蒸留塔。2. A structure in which a plurality of pipes are connected to a main body by means of a tube plate at both ends, so that the inside and outside of the plurality of pipes are separated from each other inside the main body. An inlet / outlet is provided, the inside of the pipe is set to the low pressure (recovery section) side, and the outside of the pipe is set to the high pressure (concentration section) side. An internal heat exchange type distillation column in which one distillation column is constituted by transferring heat from the outside of the high pressure side tube (concentration section) to the inside of the low pressure side pipe (recovery section) side. A quadrangular arrangement, wherein the enrichment section on the outer side of the tubes is a packed tower, and four pipes facing each other and adjacent to each other (a four-tube unit) whose lines connecting the centers form a substantially square shape when viewed in plan And a plurality of regions partitioned by lines forming the substantially square In each of the divided area), heat integrated distillation column packing (split packing) is characterized in that it is filled with a planar shape corresponding to the partitioned regions.
た充填物ブロックを複数個充填することにより、前記区
画領域に充填物を充填したことを特徴とする請求項1又
は2記載の内部熱交換型蒸留塔。3. The packing material according to claim 1, wherein the plurality of divided packings are filled with a plurality of packing blocks formed integrally with each other, so that the packing area is filled with the packing material. Internal heat exchange distillation column.
部分の間に形成される空隙には、前記充填物(分割充填
物)以外の充填物が充填されていることを特徴とする請
求項1〜3のいずれかに記載の内部熱交換型蒸留塔。4. A space formed between the inner wall of the main body and a portion of the plurality of pipes facing the main body is filled with a filler other than the filler (divided filler). The internal heat exchange type distillation column according to claim 1.
胴と連結させることにより、複数管の管内と管外が隔離
された構造とした塔(本体胴)内の、複数管の管外に充
填物を充填する場合に用いられる充填物であって、 平面的に見た場合に中心を結ぶ線が略正三角形を形成す
る互いに隣接する3本の管(三本管ユニット)の外周部
と、前記略正三角形を形成する線により区画される複数
の領域(区画領域)に対応する平面形状、又は、前記区
画領域を複数個接続した平面形状を有するように分割形
成されていることを特徴とする充填物。5. A plurality of tubes having a triangular arrangement connected to the body by means of a tube plate at both ends, so that the inside of the plurality of tubes is separated from the outside of the tube. Used to fill the filling material in the outer periphery of three adjacent pipes (three-tube unit) whose center connecting line forms a substantially equilateral triangle when viewed in a plan view. And that it is divided so as to have a planar shape corresponding to a plurality of regions (partitioned regions) defined by lines forming the substantially equilateral triangle, or a planar shape in which a plurality of the divided regions are connected. Characteristic filling.
胴と連結させることにより、複数管の管内と管外が隔離
された構造とした塔(本体胴)内の、複数管の管外に充
填物を充填する場合に用いられる充填物であって、 平面的に見た場合に中心を結ぶ線が略正方形を形成する
互いに対向・隣接する4本の管(4本管ユニット)の外
周部と、前記略正方形を形成する線により区画される複
数の領域(区画領域)に対応する平面形状、又は、前記
区画領域を複数個接続した平面形状を有するように分割
形成されていることを特徴とする充填物。6. A plurality of tubes in a tower (body shell) having a structure in which the inside of the plurality of tubes is separated from the outside of the tube by connecting the plurality of tubes in a square array to the main body by a tube plate at both ends. Which is used when the filling is performed on the outer periphery of four pipes (four pipe units) opposed to each other and adjacent to each other, the lines connecting the centers form a substantially square shape when viewed in a plan view. Part and a planar shape corresponding to a plurality of regions (partitioned regions) defined by the lines forming the substantially squares, or being divided and formed to have a planar shape in which a plurality of the divided regions are connected. Characteristic filling.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36493897A JP3155501B2 (en) | 1997-12-19 | 1997-12-19 | Internal heat exchange type distillation column and packing used for it |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36493897A JP3155501B2 (en) | 1997-12-19 | 1997-12-19 | Internal heat exchange type distillation column and packing used for it |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11179101A true JPH11179101A (en) | 1999-07-06 |
JP3155501B2 JP3155501B2 (en) | 2001-04-09 |
Family
ID=18483034
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Application Number | Title | Priority Date | Filing Date |
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JP36493897A Expired - Fee Related JP3155501B2 (en) | 1997-12-19 | 1997-12-19 | Internal heat exchange type distillation column and packing used for it |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8906141B2 (en) | 2012-08-09 | 2014-12-09 | Mitsubishi Heavy Industries, Ltd. | Carbon dioxide recovery apparatus and method |
-
1997
- 1997-12-19 JP JP36493897A patent/JP3155501B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8906141B2 (en) | 2012-08-09 | 2014-12-09 | Mitsubishi Heavy Industries, Ltd. | Carbon dioxide recovery apparatus and method |
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Publication number | Publication date |
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JP3155501B2 (en) | 2001-04-09 |
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