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JP3079092B1 - Internal heat exchange distillation column - Google Patents

Internal heat exchange distillation column

Info

Publication number
JP3079092B1
JP3079092B1 JP11029714A JP2971499A JP3079092B1 JP 3079092 B1 JP3079092 B1 JP 3079092B1 JP 11029714 A JP11029714 A JP 11029714A JP 2971499 A JP2971499 A JP 2971499A JP 3079092 B1 JP3079092 B1 JP 3079092B1
Authority
JP
Japan
Prior art keywords
pipe
tube sheet
main body
tube
tower
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP11029714A
Other languages
Japanese (ja)
Other versions
JP2000229202A (en
Inventor
一正 阿曽
俊成 中西
秀夫 野田
一史 吉田
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.)
Kansai Chemical Engineering Co Ltd
Kimura Chemical Plants Co Ltd
Maruzen Petrochemical Co Ltd
Original Assignee
Kansai Chemical Engineering Co Ltd
Kimura Chemical Plants Co Ltd
Maruzen Petrochemical Co 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 Kansai Chemical Engineering Co Ltd, Kimura Chemical Plants Co Ltd, Maruzen Petrochemical Co Ltd filed Critical Kansai Chemical Engineering Co Ltd
Priority to JP11029714A priority Critical patent/JP3079092B1/en
Application granted granted Critical
Publication of JP3079092B1 publication Critical patent/JP3079092B1/en
Publication of JP2000229202A publication Critical patent/JP2000229202A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

【要約】 【課題】 所定の位置に塔頂側管板を確実に配設、固定
し、その貫通孔に管の上端部を接続することにより、管
を高い位置精度で塔頂側管板に接続することが可能な接
続構造を有する内部熱交換型蒸留塔を提供する。 【解決手段】 塔頂側管板取付部材22を用いて本体胴
1と塔頂側管板3aを接続、固定し、管接続部材24を
用いて、管25と塔頂側管板3aを接続、固定する。ま
た、塔頂側管板取付部材22として、塔頂側管板3aの
外径よりも大きい内径を有する単管を用い、下端部を本
体胴上側フランジ部1aの上面にシール溶接し、上端部
を塔頂側管板3aの外周面にシール溶接する。また、塔
頂カバー31を、パッキン26を介して本体胴1に取り
外し可能に取り付ける。
Abstract: PROBLEM TO BE SOLVED: To securely dispose and fix a top-side tube sheet at a predetermined position, and connect an upper end portion of the tube to a through-hole thereof, so that the tube can be accurately positioned on the top-side tube sheet. Provided is an internal heat exchange type distillation column having a connection structure that can be connected. SOLUTION: A main body 1 and a top tube sheet 3a are connected and fixed using a top tube sheet attachment member 22, and a pipe 25 and a top tube sheet 3a are connected using a tube connection member 24. , Fix. In addition, a single tube having an inner diameter larger than the outer diameter of the tower-side tube sheet 3a is used as the tower-side tube sheet attaching member 22, and the lower end portion is seal-welded to the upper surface of the main body upper flange portion 1a. Is seal-welded to the outer peripheral surface of the top-side tube sheet 3a. Further, the top cover 31 is detachably attached to the main body 1 via the packing 26.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、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
交換型蒸留塔に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an internal device that includes a low-pressure column and a high-pressure column, and performs heat exchange between the high-pressure column (concentrating unit) and the low-pressure column (recovering unit) by transferring heat between the two. It 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、省エネルギーに最も忠
実な理論であることは、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 A distillation column excellent in energy saving is provided with a low-pressure column and a high-pressure column, and is configured to exchange heat between the two, and to transfer heat to and from the other. There is known an internal heat exchange type distillation column which does not require a heat exchanger. From the viewpoint of promoting the energy saving of the distillation operation, this internal heat exchange type distillation column is the most faithful theory for energy saving, and it is natural in principle,
It is being recognized from academics.

【0003】また、内部熱交換型蒸留塔として、複数管
(場合によっては単管)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)。この内部熱交換型蒸留塔
は、図1(a)及び(b)に示すような構造を有している。
[0003] Further, as an internal heat exchange type distillation column, a plurality of tubes (in some cases, a single tube) 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 inside the main body. The structure is made, and the inlet and outlet of gas and liquid are provided inside and outside the pipe, the operating temperature is made different by making the operating pressure inside and outside the pipe different, and the pipe wall of multiple pipes is used as a heat transfer surface. There has been proposed a structure in which a single distillation column is configured by transferring heat from a high pressure side to a low pressure side so that a high pressure side is a concentration section and a low pressure side is a recovery section (Japanese Patent No. 2694425). This internal heat exchange type distillation column has a structure as shown in FIGS. 1 (a) and 1 (b).

【0004】すなわち、この内部熱交換型蒸留塔は、本
体胴1と、本体胴1内に挿入された複数管(管)25を
両端管板(上側管板(塔頂側管板)3a及び下側管板
(塔底側管板)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いる。そして、複数管25の管内4
と管外5は互いに隔離された構造を有しており、管内4
が高圧側の濃縮部となり、管外5が低圧側の回収部とな
るように構成されている。ただし、管内4を低圧側の回
収部、管外5を高圧側の濃縮部とすることも可能であ
る。
That is, in this internal heat exchange type distillation column, the main body 1 and a plurality of pipes (tubes) 25 inserted into the main body 1 are connected to both ends of a tube plate (upper tube plate (tower tube plate) 3a). It is formed by being connected to the main body 1 by a lower tube sheet (tower tube sheet) 3b). And the inside 4 of the plurality of tubes 25
The outer tube 5 and the outer tube 5 have a structure isolated from each other.
Is a concentrating section on the high pressure side, and the outside tube 5 is a collecting section on the low pressure side. However, it is also possible to set the inside of the tube 4 as a low pressure side recovery unit and the outside of the tube 5 as a high pressure side concentration unit.

【0005】以下、管内4が高圧側の濃縮部、管外5が
低圧側の回収部である場合について説明を行う。
Hereinafter, a case where the inside of the pipe 4 is a concentrating section on the high pressure side and the outside of the pipe 5 is a collecting section on the low pressure side will be described.

【0006】管内(濃縮部)4には規則充填物が充填さ
れており、管外(回収部)5には不規則充填物が充填さ
れている。また、本体胴1の上部には、管外(回収部)
5に液を供給するための回収部液入口6、管外(回収
部)5からの蒸気を抜き出す回収部蒸気出口7が配設さ
れており、塔頂側管板3aより上側の、管内(濃縮部)
4と連通する端室14aには、管内(濃縮部)4に液を
供給するための濃縮部液入口8が配設され、また、管内
(濃縮部)4からの蒸気を抜き出す濃縮部蒸気出口9が
配設されている。
The inside of the tube (concentrating unit) 4 is filled with a structured packing, and the outside of the tube (collecting unit) 5 is filled with an irregular packing. In addition, outside the tube (collection unit)
A recovery section liquid inlet 6 for supplying liquid to the apparatus 5 and a recovery section vapor outlet 7 for extracting vapor from the outside of the pipe (recovery section) 5 are provided. Enrichment section)
A concentrated section liquid inlet 8 for supplying liquid to the pipe (concentrating section) 4 is provided in the end chamber 14 a communicating with the pipe 4, and a condensing section vapor outlet for extracting vapor from the pipe (concentrating section) 4. 9 are provided.

【0007】一方、本体胴1の下部には、管外(回収
部)5に蒸気を供給するための回収部蒸気入口10、管
外(回収部)5からの液を抜き出す回収部液出口11が
配設されており、塔底側管板3bより下側の、管内(濃
縮部)4と連通する端室14bには、管内(濃縮部)4
に蒸気を供給するための濃縮部蒸気入口12が配設さ
れ、また、管内(濃縮部)4からの液を抜き出す濃縮部
液出口13が配設されている。
On the other hand, at the lower part of the main body 1, a recovery section steam inlet 10 for supplying steam to the outside of the pipe (recovery section) 5, and a recovery section liquid outlet 11 for extracting liquid from the outside of the pipe (recovery section) 5. Is disposed in an end chamber 14b below the bottom tube plate 3b and communicating with the inside of the tube (concentrating unit) 4;
A vapor inlet 12 for supplying the vapor to the concentrator is provided, and a liquid outlet 13 for the liquid from the concentrator for extracting the liquid from the pipe (concentrator) 4 is provided.

【0008】ところで、上述のような、いわゆるシェル
・アンド・チューブ型の内部熱交換型蒸留塔は、一般的
に用いられているシェル・アンド・チューブ型の熱交換
器と同様の構造を有しているが、熱交換器の場合には、
通常、管(チューブ)として、長さが6m程度のものが
用いられることが多い。これに対して、内部熱交換型蒸
留塔では、管(チューブ)25として、長さが10m以
上になるものが用いられる場合が多い。また、管25内
には、蒸留部構成物(ここでは充填物であり、その他に
も棚段などが用いられる場合がある)が組み込まれるこ
とになる。
Meanwhile, the above-mentioned so-called shell and tube type internal heat exchange type distillation column has a structure similar to that of a generally used shell and tube type heat exchanger. However, in the case of a heat exchanger,
Usually, a tube having a length of about 6 m is often used. On the other hand, in the internal heat exchange type distillation column, a tube (tube) 25 having a length of 10 m or more is often used. Further, in the pipe 25, a distillation section component (here, a packing, and in addition, a tray or the like may be used) is incorporated.

【0009】ところで、上述のようなシェル・アンド・
チューブ型の内部熱交換型蒸留塔の据え付け工程で、内
部に蒸留部が組み込まれた管25を、塔底側管板3bが
本体胴1の下部に取り付けられた塔本体に組み込む場
合、まず、管25を塔頂より釣り下げて、塔底側管板3
bの管取付用の貫通孔41に挿入する。
[0009] By the way, the shell and
In the installation process of the tube-type internal heat exchange type distillation column, in the case where the pipe 25 in which the distillation section is incorporated is incorporated into the column main body in which the column bottom tube plate 3b is attached to the lower portion of the main body shell 1, first, The tube 25 is hung from the top of the tower,
Insert into the through hole 41 for mounting the pipe of b.

【0010】それから、所定のシール溶接を行って、管
25の下端側を塔底側管板3bに固定し、管25を略垂
直に立てた状態で、管外側に蒸留部を組み込む。
[0010] Then, a predetermined seal welding is performed to fix the lower end side of the tube 25 to the bottom tube plate 3b, and a distillation unit is installed on the outside of the tube while the tube 25 is set substantially vertically.

【0011】次いで、管外側に供給される液を分配する
ための管外側分配器6a(図1(a))を取り付ける。
Next, an outside distributor 6a (FIG. 1 (a)) for distributing the liquid supplied to the outside of the tube is attached.

【0012】その後、塔頂側管板3aを所定の位置に配
設し、管25の上端部を塔頂側管板3aの貫通孔に接続
した後、塔頂側管板3aとの間に塔頂側の端室14aを
形成する塔頂カバー31を取り付けることにより、図1
に示すような構造を有する内部熱交換型蒸留塔が得られ
る。
Thereafter, the top-side tube sheet 3a is arranged at a predetermined position, and the upper end of the pipe 25 is connected to a through hole of the top-side tube sheet 3a. By attaching the top cover 31 forming the end chamber 14a on the top side, FIG.
An internal heat exchange type distillation column having a structure as shown in FIG.

【0013】しかし、所定の位置に塔頂側管板3aを配
設、固定するとともに、複数の貫通孔21のそれぞれに
所定の管25の上端部を接続したり、塔頂カバー31を
取り付けたりする作業は、管25の位置精度などが蒸留
塔の性能に大きく影響することから、所望の蒸留特性を
確保しようとすると高い位置精度が要求されることにな
り、必ずしも容易ではない。
However, the top-side tube sheet 3a is arranged and fixed at a predetermined position, and the upper end of a predetermined tube 25 is connected to each of the plurality of through holes 21 or the top cover 31 is attached. Since the positional accuracy of the pipe 25 greatly affects the performance of the distillation column, a high positional accuracy is required to secure desired distillation characteristics, which is not always easy.

【0014】本発明は、上記問題点を解決するものであ
り、所定の位置に塔頂側管板を確実に配設、固定し、そ
の貫通孔に管の上端部を接続することにより、管を高い
位置精度で塔頂側管板に接続するとともに、塔頂カバー
を容易に取り付けることが可能な構造を有する内部熱交
換型蒸留塔を提供することを目的とする。
The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to dispose and fix a tower-side tube sheet at a predetermined position and connect an upper end portion of the tube to a through hole thereof. Is connected to the top-side tube sheet with high positional accuracy, and an internal heat exchange type distillation column having a structure in which a top cover can be easily attached is provided.

【0015】[0015]

【課題を解決するための手段】上記目的を達成するため
に、本発明(請求項1)の内部熱交換型蒸留塔は、本体
胴内に配設された単管又は複数管(以下、単に「管」と
いう)を、塔頂側及び塔頂側の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、管の
内部(管内)と管の外部(管外)が隔離された構造と
し、前記管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、前
記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、高圧側が濃縮部、低圧側が回収部と
して機能するように構成された内部熱交換型蒸留塔であ
って、 (a) 塔頂側管板の外径よりも大きい内径を有する単管
状の塔頂側管板取付部材の内側に、塔頂側管板がはまり
込むとともに、塔頂側管板の周辺部の下面が本体胴上側
フランジ部の上面に当接するように配設され、 (b)前記塔頂側管板取付部材の下端側の全周が、塔頂側
端室を形成する塔頂カバーと本体胴とを接続するための
本体胴上側フランジ部にシール溶接され、かつ、前記塔
頂側管板取付部材の上端側の全周が、塔頂側管板にシー
ル溶接されるこ とにより、 塔頂側管板が塔頂側管板取付
部材を介して本体胴に取り付けられているとともに、 ()塔頂側管板の、管取付用の貫通孔に、前記管の上端
部が挿入され、 ()前記管が挿通される挿通穴を備えた管接続部材が、
塔頂側管板の上面側から塔頂側管板の貫通孔の内周と管
の外周の間の隙間を封止するように管の上端部にはめ込
まれ、かつ、 ()管と管接続部材をシール溶接するとともに、管接続
部材と塔頂側管板をシール溶接することにより、管が管
接続部材を介して塔頂側管板に接続されていることを特
徴としている。
In order to achieve the above object, an internal heat exchange type distillation column of the present invention (Claim 1) comprises a single tube or a plurality of tubes (hereinafter simply referred to as a single tube) disposed inside a main body. The pipe is connected to the main body by means of the top and the both ends of the pipe at the top, so that the inside of the pipe (inside the pipe) and the outside of the pipe (outside the pipe) are isolated inside the main body. The pipe is provided with a gas-liquid inlet and outlet, and the operating temperature is made different by making a difference in the operating pressure between the inside and the outside of the pipe, and the pipe wall of the pipe is used as a heat transfer surface, from the high pressure side to the low pressure side. The heat transfer to the internal heat exchange type distillation column configured such that the high pressure side functions as a concentration section and the low pressure side functions as a recovery section, and (a) an inner diameter larger than the outer diameter of the top-side tube sheet. Single tube with
The top tubesheet fits inside the top-side tubesheet mounting member
And the lower surface of the periphery of the top tubesheet
Is disposed so as to contact the upper surface of the flange portion, (b) the entire circumference of the lower end of the tower top side tube plate mounting member, the top side
For connecting the top cover forming the end chamber with the main body
Seal welding is performed on the upper flange of the main body, and the tower is
The entire circumference of the upper end of the top tube sheet mounting member is sealed to the top tube sheet.
By the This is Le welded, together with the top side tube plate is attached to the body trunk via the column top side tube plate mounting member, (c) the top side tube plate, the through hole for the tube mounting ( D ) a pipe connection member having an insertion hole through which the pipe is inserted,
( E ) The pipe and the pipe are fitted into the upper end of the pipe so as to seal a gap between the inner circumference of the through hole of the tower pipe and the outer circumference of the pipe from the top side of the top tubesheet. The pipe is connected to the top tubesheet via the pipe connection member by seal-welding the connection member and seal-welding the pipe connection member and the top tubesheet.

【0016】本体胴と塔頂側管板、管と塔頂側管板の接
続構造を、上述の(a),(b),(c),(d),(e)の要件
を備えた構造とした場合、塔頂側管板取付部材を介し
て、塔頂側管板が本体胴の所定の位置に確実に固定され
るとともに、管接続部材を介して、管の上端部が塔頂側
管板の貫通孔に確実に接続されることになる。すなわ
ち、塔頂側管板取付部材を介して塔頂側管板を所定の位
置に固定した状態で、管の上端部が塔頂側管板の貫通孔
に管接続部材を介して接続されることになるため、管を
所望の蒸留性能を得ることが可能な位置に容易かつ確実
に配設することが可能になり、内部熱交換型蒸留塔を効
率よく組み立てることが可能になる。
The connection structure between the main body and the top tubesheet, and the connection structure between the tubes and the top tubesheet satisfy the above-mentioned requirements (a), (b), (c), (d) and (e) . In the case of a structure, the top-side tube sheet is securely fixed to a predetermined position of the main body via the top-side tube sheet mounting member, and the top end of the pipe is connected to the top via the pipe connection member. It is surely connected to the through hole of the side tube sheet. That is, the upper end of the pipe is connected to the through-hole of the top-side tube sheet via the pipe connection member while the top-side tube sheet is fixed at a predetermined position via the top-side tube sheet attachment member. Therefore, it is possible to easily and reliably arrange the tube at a position where a desired distillation performance can be obtained, and it is possible to efficiently assemble the internal heat exchange type distillation column.

【0017】また、請求項2の内部熱交換型蒸留塔は、
前記塔頂側管板取付部材が、塔頂側管板の外径よりも大
きい内径を有し、塔頂側管板が内側にはまり込む単管で
あって、下端部が、本体胴上側フランジ部の上面にシー
ル溶接されているとともに、上端部が、塔頂側管板取付
部材の内側にはまり込んで周辺部の下面が本体胴上側フ
ランジ部の上面に当接するように配設された塔頂側管板
の外周面にシール溶接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 comprises:
The top-side tube sheet mounting member has a larger inner diameter than the outer diameter of the top-side tube sheet, and is a single tube in which the top-side tube sheet fits inside, and the lower end portion is a main body upper flange. The upper end of the tower is fitted with a seal welded to the upper surface of the upper portion, and the upper end is fitted inside the tower-side tubesheet mounting member, and the lower surface of the peripheral portion is arranged to contact the upper surface of the upper flange portion of the main body trunk. It is characterized by being seal-welded to the outer peripheral surface of the top tube sheet.

【0018】塔頂側管板取付部材として、塔頂側管板の
外径よりも大きい内径を有する単管を用い、下端部を本
体胴上側フランジ部の上面にシール溶接し、上端部を塔
頂側管板の外周面にシール溶接するようにした場合、塔
頂側管板を本体胴の所定の位置に容易かつ確実に取り付
けることが可能になり、本発明をより実効あらしめるこ
とができる。
A single tube having an inner diameter larger than the outer diameter of the top tubesheet is used as the top tubesheet mounting member, and the lower end is seal-welded to the upper surface of the main body upper flange, and the upper end is attached to the tower. When seal welding is performed on the outer peripheral surface of the top tube sheet, the tower tube sheet can be easily and reliably attached to a predetermined position of the main body, and the present invention can be made more effective. .

【0019】また、請求項3の内部熱交換型蒸留塔は、
前記管接続部材が、単管状で、上端側に、外径が塔頂側
管板の貫通孔の直径よりも大きいフランジ部を備えた構
造を有していることを特徴としている。
The internal heat exchange type distillation column according to claim 3 is characterized in that:
The pipe connection member is characterized in that it is a single tube, and has a structure provided with a flange on the upper end side, the outer diameter of which is larger than the diameter of the through-hole of the tower-side tube sheet.

【0020】管接続部材として、単管状で、上端側に、
外径が塔頂側管板の貫通孔の直径よりも大きいフランジ
部を備えた構造のものを用いた場合、下端部を管と塔頂
側管板の貫通孔の隙間にはまり込ませた状態で、管と管
接続部材をシール溶接し、かつ、塔頂側管板の貫通孔の
周囲と管接続部材をシール溶接することにより、管を塔
頂側管板の貫通孔に、管接続部材を介して容易かつ確実
に接続することが可能になる。
As a pipe connecting member, it is a single tube, and on the upper end side,
When using a structure with a flange whose outer diameter is larger than the diameter of the through-hole of the top-side tube sheet, the lower end is fitted into the gap between the pipe and the through-hole of the top-side tube sheet Then, the pipe and the pipe connection member are seal-welded, and the periphery of the through hole of the tower-side tube sheet and the pipe connection member are seal-welded, so that the pipe is connected to the through-hole of the tower-side tube sheet, thereby forming the pipe connection member. It is possible to easily and surely connect via.

【0021】また、請求項4の内部熱交換型蒸留塔は、
塔頂側管板の上面側に配設され、塔頂側管板との間に塔
頂側端室を形成する塔頂カバーが、パッキンを介して本
体胴に取り外し可能に取り付けら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 4 comprises:
A top cover, which is disposed on the top side of the top tube sheet and forms a top end chamber between the top tube sheet and the top tube sheet, is detachably attached to the main body via packing. It is characterized by.

【0022】塔頂カバーを、パッキンを介して本体胴に
取り外し可能に取り付けるようにした場合、必要に応じ
て内部熱交換型蒸留塔を容易に分解することが可能にな
り、メンテナンスなどの容易化を図ることが可能にな
る。なお、塔頂カバーを着脱可能に取り付けるようにし
た場合にも、塔頂側管板が、塔頂側管板取付部材を介し
て、本体胴に固定されているため、蒸留性能に悪影響を
及ぼすような管の位置ずれを招くことはない。
When the top cover is detachably attached to the main body via a packing, the internal heat exchange type distillation column can be easily disassembled as required, and maintenance and the like can be simplified. Can be achieved. Even when the top cover is detachably attached, the distillation performance is adversely affected because the top tube sheet is fixed to the main body via the top tube sheet mounting member. Such a displacement of the tube does not occur.

【0023】[0023]

【発明の実施の形態】以下、本発明の実施の形態を示し
て、その特徴とするところを詳しく説明する。図1(a)
は本発明の一実施形態にかかる内部熱交換型蒸留塔を示
す正面断面図、図1(b)はそのb−b線断面図であり、
また、図2は、図1(a)において一点鎖線で囲んだ部分
Aの構造を示す拡大図である。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described, and features thereof will be described in detail. FIG. 1 (a)
1 is a front sectional view showing an internal heat exchange type distillation column according to one embodiment of the present invention, FIG.
FIG. 2 is an enlarged view showing a structure of a portion A surrounded by a dashed line in FIG.

【0024】図1(a)及び(b)の内部熱交換型蒸留塔の
構成については、従来の技術及び発明が解決しようとす
る課題の欄ですでに説明されていることから、重複を避
けるため、ここでは内部熱交換型蒸留塔全体の構成につ
いての説明を省略し、本発明の特徴部分について詳しく
説明する。
The structure of the internal heat exchange type distillation column shown in FIGS. 1A and 1B has been already described in the section of the prior art and the problem to be solved by the invention, so that duplication is avoided. Therefore, the description of the configuration of the entire internal heat exchange type distillation column is omitted here, and the features of the present invention will be described in detail.

【0025】以下、この実施形態の内部熱交換型蒸留塔
の特徴部分である、複数管(管)25の上端部の塔頂側
管板への接続構造(図1(a)の一点鎖線で囲んだ部分A
の構造)について、図2を参照しつつ説明する。
Hereinafter, a connection structure of the upper end portion of the plurality of tubes (tubes) 25 to the top tube plate, which is a characteristic portion of the internal heat exchange type distillation column of this embodiment (shown by a dashed line in FIG. Surrounded part A
Will be described with reference to FIG.

【0026】この内部熱交換型蒸留塔においては、塔頂
側管板3aとの間に塔頂側端室14a(図1(a))を形
成する塔頂カバー31と本体胴1とを接続するための本
体胴上側のフランジ部1aに、塔頂側管板取付部材22
の下端部を全周にわたってシール溶接するとともに、塔
頂側管板取付部材22の上端部を、塔頂側管板3aの外
周面の全周にわたってシール溶接することにより、塔頂
側管板3aが塔頂側管板取付部材22を介して本体胴1
に取り付けられている。すなわち、塔頂側管板取付部材
22の下端部が全周にわたって本体胴1の上側のフラン
ジ部1aの上面にシール溶接され、上端部が、塔頂側管
板3aの外周面にシール溶接されており、塔頂側管板3
aが、塔頂側管板取付部材22を介して、本体胴1の所
定の位置に確実に取り付けられている。
In this internal heat exchange type distillation column, a top cover 31 forming a top end chamber 14a (FIG. 1 (a)) and a main body 1 are connected to a top tube plate 3a. The top tubesheet mounting member 22 is attached to the flange portion 1a
Is welded over the entire circumference and the upper end of the top-side tube sheet mounting member 22 is seal-welded over the entire outer circumferential surface of the top-side tube sheet 3a, thereby forming the top-side tube sheet 3a. Is connected to the main body 1 via the top-side tube sheet mounting member 22.
Attached to. That is, the lower end of the tower-side tube sheet mounting member 22 is seal-welded to the upper surface of the upper flange portion 1a of the main body 1 over the entire circumference, and the upper end is seal-welded to the outer peripheral surface of the tower-side tube sheet 3a. And the top tubesheet 3
a is securely attached to a predetermined position of the main body 1 through the tower-side tube sheet attachment member 22.

【0027】また、塔頂側管板3aの管25が取り付け
られる貫通孔21には管25の上端部が挿入されてお
り、管接続部材24を介して、管25の上端部が塔頂側
管板3aの貫通孔21に固定されている。この実施形態
では、管接続部材24として、単管状で、上端側に、外
径が塔頂側管板3aの貫通孔21の直径よりも大きいフ
ランジ部24aを備えた構造のものが用いられており、
その下端部24bを塔頂側管板3aの貫通孔21と管2
5の隙間23にはまり込ませた状態で、管25と管接続
部材24をシール溶接するとともに、管接続部材24と
塔頂側管板3aの貫通孔21の周囲部分とをシール溶接
することにより、管25が管接続部材24を介して塔頂
側管板3aの貫通孔21に接続されている。
The upper end of the tube 25 is inserted into the through hole 21 of the tower tube plate 3a where the tube 25 is attached. It is fixed to the through hole 21 of the tube sheet 3a. In this embodiment, a pipe connecting member 24 having a single-tube structure having a flange portion 24a having an outer diameter larger than the diameter of the through hole 21 of the tower-side tube sheet 3a at the upper end is used. Yes,
The lower end 24b is connected to the through-hole 21 of the top-side tube sheet 3a and the pipe 2
5, while the pipe 25 and the pipe connecting member 24 are seal-welded while the pipe connecting member 24 and the peripheral portion of the through-hole 21 of the tower-side tube sheet 3a are sealed and welded. , A pipe 25 is connected to the through-hole 21 of the tower-side tube sheet 3 a via a pipe connecting member 24.

【0028】また、塔頂カバー31は、塔頂カバー31
の下端部に設けられたフランジ部31aと塔頂側管板3
aの上面の間にパッキン26を挟み込み、塔頂カバー3
1のフランジ部31aと本体胴1の上側のフランジ部1
aをボルト(図示せず)で締結することにより取り外す
ることができるように本体胴1に取り付けられている。
Further, the top cover 31 is
31a provided at the lower end of the tower and the top-side tubesheet 3
a between the upper surfaces of the top cover 3
1 flange portion 31a and upper flange portion 1 of main body 1
a is attached to the main body 1 so that it can be removed by fastening it with a bolt (not shown).

【0029】次に、管25の上端部を塔頂側管板3aに
接続する方法について説明する。なお、ここでは、図1
に示すように、内部に蒸留部が配設された管25の下端
側を塔底側管板3bに固定し、管25を略垂直に立てた
状態で、管外側に蒸留部を組み込み、管外側分配器6a
を取り付けた後、塔頂側管板3aを配設する工程以降の
工程について説明する。塔頂側管板3aを本体胴1の
上部の所定の位置に置く。このとき、管25の上端部
が、塔頂側管板3aの各貫通孔21にはまり込む。な
お、塔頂側管板3aの貫通孔21は、管25の外径より
十分に大きくしておく。塔底側管板3bの貫通孔41
は、管25の位置を定めるために、管25の外径+1mm
程度でよいが、塔頂側管板3aの貫通孔21は、管25
の外径+15mm程度とする。これは、管25の長さが1
0m以上の長さとなることが多く、塔頂の管中心が必ず
しも塔底の管中心の垂直上にない場合が多いことによ
る。なお、内部熱交換型蒸留塔では、塔底と塔頂で管2
5の径が異なる場合のほうが多い。なお、塔頂側管板取
付部材22は、予め本体胴1の上側のフランジ部1aに
溶接付けしておいてもよく、また、塔頂側管板3aを置
いた後、塔頂側管板取付部材22を本体胴1のフランジ
部1aに溶接するようにしてもよい。また、製造工場に
おいて内部熱交換型蒸留塔本体の圧力テストを行う場合
のテスト法、据え付け場所への輸送法、現地据え付け時
の塔垂直度の認定法などにより、先に塔頂側管板取付部
材22を溶接付けしているとテストや輸送、あるいは垂
直度の認定の妨げとなる場合があるが、現地工事期間を
短縮するためには予め溶接付けを行っておくことが望ま
しい。それゆえ、上記の諸般の事情を考慮して塔頂側管
板取付部材22の取付時点を決定することが望ましい。
次に、塔頂側管板3aと本体胴1の上側のフランジ部
1aの当たり面に、塔頂カバー31のフランジ部31a
と本体胴1の上側のフランジ部1aをボルト締めした場
合に加わるのと同程度の接圧を、万力などの治具を用い
て加え、その状態で塔頂側管板取付部材22と塔頂側管
板3aをシール溶接する。それから、管接続部材24
を管25のそれぞれに1つずつ取り付ける。そして、
管接続部材24と塔頂側管板3をシール溶接するととも
に、管接続部材24と管25をシール溶接する。その
後、上記で用いた万力などの治具を取り外し、管内用
の塔頂還流分配器8a(図1(a))を取り付ける。そ
れから、パッキン26を介して、塔頂カバー31をセッ
トし、ボルト(図示せず)を締結する。
Next, a method of connecting the upper end of the pipe 25 to the top-side tube sheet 3a will be described. Here, FIG.
As shown in (2), the lower end of the tube 25 in which the distillation unit is disposed is fixed to the bottom tube plate 3b, and the distillation unit is installed outside the tube in a state where the tube 25 is set up substantially vertically. Outer distributor 6a
After mounting, the steps after the step of disposing the top-side tube sheet 3a will be described. The top-side tube sheet 3 a is placed at a predetermined position on the upper part of the main body 1. At this time, the upper end of the pipe 25 fits into each through-hole 21 of the tower-side tube sheet 3a. The through-hole 21 of the top-side tube sheet 3a is sufficiently larger than the outer diameter of the tube 25. Through-hole 41 in tower tube 3b
Is the outer diameter of the tube 25 + 1 mm to determine the position of the tube 25
The through-hole 21 of the top-side tube sheet 3a is
Outside diameter + about 15 mm. This means that the length of the tube 25 is 1
This is because the length is often 0 m or more, and the center of the column at the top of the column is not necessarily vertically above the center of the column at the bottom of the column. In addition, in the internal heat exchange type distillation column, pipes 2
More often, the diameters of 5 are different. The top-side tube sheet mounting member 22 may be welded to the upper flange portion 1a of the main body 1 in advance, or after the top-side tube sheet 3a is placed, the top-side tube sheet is attached. The attachment member 22 may be welded to the flange portion 1a of the main body 1. In addition, the top tube plate is installed first according to the test method for conducting the pressure test of the internal heat exchange type distillation column body at the manufacturing plant, the transportation method to the installation location, the certification method of the tower verticality at the time of installation on site, etc. If the member 22 is welded, it may hinder testing, transportation, or recognition of verticality, but it is desirable to perform welding in advance in order to shorten the on-site construction period. Therefore, it is desirable to determine the mounting time of the tower-side tube sheet mounting member 22 in consideration of the above various circumstances.
Next, on the contact surface between the top-side tube sheet 3a and the upper flange portion 1a of the main body 1, a flange portion 31a of the top cover 31 is provided.
And a jig such as a vise, applying a contact pressure similar to that applied when the upper flange portion 1a of the main body 1 is bolted. The top tube sheet 3a is seal-welded. Then, the pipe connecting member 24
Is attached to each of the tubes 25 one by one. And
The pipe connecting member 24 and the tower-side tube sheet 3 are seal-welded, and the pipe connecting member 24 and the pipe 25 are seal-welded. Thereafter, the jig such as the vise used above is removed, and the tower top reflux distributor 8a (FIG. 1 (a)) is attached. Then, the top cover 31 is set via the packing 26, and bolts (not shown) are fastened.

【0030】これにより、図2に示すような、管25の
塔頂側管板3aへの接続構造を有する内部熱交換型蒸留
塔(図1)が完成する。
Thus, an internal heat exchange type distillation column (FIG. 1) having a structure for connecting the tube 25 to the top tube plate 3a as shown in FIG. 2 is completed.

【0031】管25と塔頂側管板3aの接続構造を、上
述のような構造とすることにより、塔頂側管板取付部材
22を介して、塔頂側管板3aが本体胴1の所定の位置
に確実に固定されるとともに、管接続部材24を介し
て、管25の上端部が塔頂側管板3aの貫通孔21に確
実に接続される。したがって、管25を所定の位置に容
易かつ確実に配設することが可能になり、所望の蒸留性
能を得ることが可能な内部熱交換型蒸留塔を効率よく組
み立てることができる。
By making the connection structure between the pipe 25 and the top-side tube sheet 3a as described above, the top-side tube sheet 3a is connected to the main body 1 via the top-side tube sheet mounting member 22. The pipe 25 is securely fixed at a predetermined position, and the upper end of the pipe 25 is reliably connected to the through-hole 21 of the tower-side tube sheet 3a via the pipe connecting member 24. Therefore, it is possible to easily and surely arrange the tube 25 at a predetermined position, and it is possible to efficiently assemble the internal heat exchange type distillation column capable of obtaining a desired distillation performance.

【0032】なお、上記実施形態では、管25内の蒸留
部として規則充填物を用いた場合について説明したが、
不規則充填物を用いる場合にも本発明を適用することが
可能である。
In the above embodiment, the case where the structured packing is used as the distillation unit in the pipe 25 has been described.
The present invention can be applied to a case where an irregular packing is used.

【0033】また、上記実施形態では、塔頂側管板取付
部材22が長さのごく短い単管であり、管接続部材24
が単管状で、上端側に外径が塔頂側管板3aの貫通孔2
1の直径よりも大きいフランジ部24aを備えた構造の
ものを用いた場合について説明したが、塔頂側管板取付
部材22及び管接続部材24の形状、構造はこれに限定
されるものではなく、その他の種々の形状とすることが
可能である。
In the above embodiment, the tower-side tube sheet mounting member 22 is a single tube having a very short length.
Is a single tube, and the outer diameter of the through hole 2 in the top-side tube sheet 3a
Although the case where the structure provided with the flange portion 24a larger than the diameter of 1 is used has been described, the shapes and structures of the tower-side tube sheet mounting member 22 and the tube connecting member 24 are not limited thereto. , And other various shapes are possible.

【0034】また、本発明は、さらにその他の点におい
ても上記実施形態に限定されるものではなく、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。
The present invention is not limited to the above embodiment in other respects, and various applications and modifications can be made within the scope of the present invention.

【0035】[0035]

【発明の効果】上述のように、本発明(請求項1)の内
部熱交換型蒸留塔は、塔頂側管板取付部材及び管接続部
材を用いて、本体胴と塔頂側管板、及び管と塔頂側管板
を接続するようにしているので、塔頂側管板取付部材を
介して、塔頂側管板を本体胴の所定の位置に確実に固定
するとともに、管接続部材を介して、管の上端部を塔頂
側管板の貫通孔に確実に接続することが可能になる。そ
の結果、管を所望の蒸留性能を得ることが可能な位置に
容易かつ確実に配設することが可能になり、内部熱交換
型蒸留塔を効率よく組み立てることができるようにな
る。
As described above, the internal heat exchange type distillation column of the present invention (Claim 1) uses the column top mounting member and the tube connecting member to form the main body and the column top tube sheet. And the pipe and the top-side tube sheet are connected, so that the top-side tube sheet is securely fixed to a predetermined position of the main body via the top-side tube sheet mounting member, and the pipe connection member Through this, it is possible to reliably connect the upper end of the pipe to the through hole of the top-side tube sheet. As a result, it is possible to easily and surely arrange the pipe at a position where a desired distillation performance can be obtained, and it is possible to efficiently assemble the internal heat exchange type distillation column.

【0036】また、請求項2の内部熱交換型蒸留塔のよ
うに、塔頂側管板取付部材として、塔頂側管板の外径よ
りも大きい内径を有する単管を用い、下端部を本体胴上
側フランジ部の上面にシール溶接し、上端部を塔頂側管
板の外周面にシール溶接するようにした場合、塔頂側管
板を本体胴に容易かつ確実に取り付けることが可能にな
り、本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 of the second aspect, a single tube having an inner diameter larger than the outer diameter of the top tube plate is used as the top tube plate mounting member, and the lower end portion is formed. When the upper end of the main body is sealed and welded to the upper surface of the upper flange, and the upper end is welded to the outer peripheral surface of the top tube, the top tube can be easily and securely attached to the main body. Thus, the present invention can be made more effective.

【0037】また、請求項3の内部熱交換型蒸留塔のよ
うに、管接続部材として、単管状で、上端側に、外径が
塔頂側管板の貫通孔の直径よりも大きいフランジ部を備
えた構造のものを用いた場合、下端部を管と貫通孔の隙
間にはまり込ませた状態で、管と管接続部材をシール溶
接し、かつ、塔頂側管板の貫通孔の周囲と管接続部材を
シール溶接することにより、管を塔頂側管板の貫通孔
に、管接続部材を介して容易かつ確実に接続することが
可能になる。
Further, as in the internal heat exchange type distillation column according to the third aspect, the pipe connection member is a single tube and has a flange portion having an outer diameter larger than the diameter of the through hole of the top tube plate at the upper end side. In the case of using a structure having a pipe, the pipe and the pipe connection member are seal-welded with the lower end portion fitted in the gap between the pipe and the through-hole, and the periphery of the through-hole in the top-side tube sheet is provided. By seal-welding the pipe connection member and the pipe connection member, the pipe can be easily and reliably connected to the through hole of the tower-side tube sheet via the pipe connection member.

【0038】また、請求項4の内部熱交換型蒸留塔のよ
うに、塔頂カバーが、パッキンを介して本体胴に取り外
し可能に取り付けるようにした場合、必要に応じて内部
熱交換型蒸留塔を容易に分解することが可能になり、メ
ンテナンスなどの容易化を図ることが可能になる。
When the top cover is detachably attached to the main body via a packing as in the internal heat exchange type distillation column according to claim 4, the internal heat exchange type distillation column may be used if necessary. Can be easily disassembled, and maintenance and the like can be facilitated.

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

【図1】本発明の一実施形態にかかる内部熱交換型蒸留
塔を示す図であり、(a)は正面断面図、(b)は(a)のb
−b線断面図である。
FIG. 1 is a diagram showing an internal heat exchange type distillation column according to an embodiment of the present invention, wherein (a) is a front sectional view, and (b) is b in (a).
It is a -b line sectional view.

【図2】本発明の一実施形態にかかる内部熱交換型蒸留
塔の要部の構成を示す正面断面図である。
FIG. 2 is a front sectional view showing a configuration of a main part of an internal heat exchange type distillation column according to one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 本体胴 1a 本体胴のフランジ部 3a 塔頂側管板(上側管板) 3b 塔底側管板(下側管板) 4 管内(濃縮部) 5 管外(回収部) 6 回収部液入口 6a 管外側分配器 7 回収部蒸気出口 8 濃縮部液入口 8a 管内用の塔頂還流分配器 9 濃縮部蒸気出口 10 回収部蒸気入口 11 回収部液出口 12 濃縮部蒸気入口 13 濃縮部液出口 14a,14b 端室 21 塔頂側管板の貫通孔 22 塔頂側管板取付部材 23 塔頂側管板の貫通孔と管の隙間 24 管接続部材 24a 管接続部材のフランジ部 24b 管接続部材の下端部 25 管(複数管) 26 パッキン 31 塔頂カバー 31a 塔頂カバーのフランジ部 41 塔底側管板の貫通孔 DESCRIPTION OF SYMBOLS 1 Main body trunk 1a Flange part of main body 3a Tower tube sheet (upper tube sheet) 3b Tower tube sheet (lower tube sheet) 4 Inside pipe (concentrating section) 5 Outside pipe (recovering section) 6 Liquid inlet in collecting section 6a Outer pipe distributor 7 Recovery section vapor outlet 8 Concentration section liquid inlet 8a Tower top reflux distributor 9 Concentration section vapor outlet 10 Recovery section vapor inlet 11 Recovery section liquid outlet 12 Concentration section vapor inlet 13 Concentration section liquid outlet 14a , 14b End chamber 21 Tower-side tube sheet through-hole 22 Tower-side tube sheet mounting member 23 Gap between through-hole of tower-side tube sheet and pipe 24 Pipe connecting member 24a Flange portion of pipe connecting member 24b Pipe connecting member Lower end 25 Pipes (multiple pipes) 26 Packing 31 Tower cover 31a Flange part of tower cover 41 Through-hole of tower plate at bottom

───────────────────────────────────────────────────── 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 吉田 一史 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 (56)参考文献 特開 平8−66601(JP,A) 実公 平7−22609(JP,Y2) 実公 昭49−36279(JP,Y1) (58)調査した分野(Int.Cl.7,DB名) B01D 3/26 - 3/28 B01D 3/32 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Toshinari Nakanishi 2-1-2, Kuisejijima, Amagasaki City, Hyogo Prefecture Inside Kimura Kakoki Co., Ltd. (72) Inventor Hideo Noda 2-97-7 Minami-Nanamatsucho, Amagasaki City, Hyogo No. Kansai Chemical Machinery Co., Ltd. (72) Inventor Kazufumi Yoshida 2-25-10 Hatchobori, Chuo-ku, Tokyo Inside Maruzen Petrochemical Co., Ltd. (56) References JP-A-8-66601 (JP, A) 7-22609 (JP, Y2) 49-36279 (JP, Y1) (58) Field surveyed (Int. Cl. 7 , DB name) B01D 3/26-3/28 B01D 3/32

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】本体胴内に配設された単管又は複数管(以
下、単に「管」という)を、塔頂側及び塔低側の両端管
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、管の内部(管内)と管の外部(管外)が隔
離された構造とし、 前記管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、 前記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、高圧側が濃縮部、低圧側が回収部
として機能するように構成された内部熱交換型蒸留塔で
あって、 (a)塔頂側管板の外径よりも大きい内径を有する単管状
の塔頂側管板取付部材の内側に、塔頂側管板がはまり込
むとともに、塔頂側管板の周辺部の下面が本体胴上側フ
ランジ部の上面に当接するように配設され、 (b)前記塔頂側管板取付部材の下端側の全周が、塔頂側
端室を形成する塔頂カバーと本体胴とを接続するための
本体胴上側フランジ部にシール溶接され、かつ、前記塔
頂側管板取付部材の上端側の全周が、塔頂側管板にシー
ル溶接されることにより、 塔頂側管板が塔頂側管板取付
部材を介して本体胴に取り付けられているとともに、 ()塔頂側管板の、管取付用の貫通孔に、前記管の上端
部が挿入され、 ()前記管が挿通される挿通穴を備えた管接続部材が、
塔頂側管板の上面側から塔頂側管板の貫通孔の内周と管
の外周の間の隙間を封止するように管の上端部にはめ込
まれ、かつ、 ()管と管接続部材をシール溶接するとともに、管接続
部材と塔頂側管板をシール溶接することにより、管が管
接続部材を介して塔頂側管板に接続されていることを特
徴とする内部熱交換型蒸留塔。
The present invention is characterized in that a single pipe or a plurality of pipes (hereinafter, simply referred to as "tubes") disposed in a main body are connected to the main body by means of both end plate plates on the top and bottom sides. Inside the body, the inside of the pipe (inside the pipe) and the outside of the pipe (outside of the pipe) are separated from each other, and the pipe is provided with a gas-liquid inlet and outlet. An internal heat exchange type in which the operating temperature is varied and the pipe wall of the pipe is used as a heat transfer surface and heat is transferred from the high pressure side to the low pressure side so that the high pressure side functions as a concentrating unit and the low pressure side functions as a recovery unit. A distillation column, (a) a single tube having an inner diameter larger than the outer diameter of the top tubesheet;
The top tubesheet fits inside the top tubesheet mounting member
In addition, the lower surface of the periphery of the top tubesheet is
Is disposed so as to contact the upper surface of the flange portion, the entire periphery of the lower end of (b) the column top side tube plate attaching member, the top side
For connecting the top cover forming the end chamber with the main body
Seal welding is performed on the upper flange of the main body, and the tower is
The entire circumference of the upper end of the top tube sheet mounting member is sealed to the top tube sheet.
The top tube sheet is attached to the main body via the top tube sheet mounting member by welding , and ( c ) the through hole for the tube attachment of the top tube sheet is ( D ) a pipe connection member having an insertion hole through which the pipe is inserted,
( E ) The pipe and the pipe are fitted into the upper end of the pipe so as to seal a gap between the inner circumference of the through hole of the tower pipe and the outer circumference of the pipe from the top side of the top tubesheet. Internal heat exchange characterized in that the pipe is connected to the top tubesheet through the pipe connection member by seal welding the connection member and seal welding the pipe connection member and the top tubesheet. Type distillation column.
【請求項2】前記塔頂側管板取付部材が、塔頂側管板の
外径よりも大きい内径を有し、塔頂側管板が内側にはま
り込む単管であって、 下端部が、本体胴上側フランジ部の上面にシール溶接さ
れているとともに、 上端部が、塔頂側管板取付部材の内側にはまり込んで周
辺部の下面が本体胴上側フランジ部の上面に当接するよ
うに配設された塔頂側管板の外周面にシール溶接されて
いることを特徴とする請求項1記載の内部熱交換型蒸留
塔。
2. The tower-side tube sheet mounting member is a single tube having an inner diameter larger than the outer diameter of the tower-side tube sheet, wherein the tower-side tube sheet fits inside, and a lower end portion is formed. , So that the upper end is fitted into the inside of the tower-side tube sheet mounting member and the lower surface of the peripheral portion is in contact with the upper surface of the upper body flange. 2. The internal heat exchange type distillation column according to claim 1, wherein a seal welding is performed on an outer peripheral surface of the disposed top-side tube sheet.
【請求項3】前記管接続部材が、単管状で、上端側に、
外径が塔頂側管板の貫通孔の直径よりも大きいフランジ
部を備えた構造を有している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 pipe connecting member is a single tube, and is provided on an upper end side thereof.
2. A structure having a flange portion having an outer diameter larger than a diameter of a through hole of a top tubesheet.
Or the internal heat exchange type distillation column according to 2.
【請求項4】塔頂側管板の上面側に配設され、塔頂側管
板との間に塔頂側端室を形成する塔頂カバーが、パッキ
ンを介して本体胴に取り外し可能に取り付けられている
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 top cover, which is disposed on the upper surface side of the top tube sheet and forms a top end chamber with the top tube sheet, is detachably attached to the main body via a packing. The internal heat exchange type distillation column according to any one of claims 1 to 3, which is attached.
JP11029714A 1999-02-08 1999-02-08 Internal heat exchange distillation column Expired - Fee Related JP3079092B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11029714A JP3079092B1 (en) 1999-02-08 1999-02-08 Internal heat exchange distillation column

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11029714A JP3079092B1 (en) 1999-02-08 1999-02-08 Internal heat exchange distillation column

Publications (2)

Publication Number Publication Date
JP3079092B1 true JP3079092B1 (en) 2000-08-21
JP2000229202A JP2000229202A (en) 2000-08-22

Family

ID=12283790

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3079092B1 (en)

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TWI398289B (en) * 2010-11-26 2013-06-11 Tseng Tung Hung Liquid distillation and purifying device
US8906141B2 (en) 2012-08-09 2014-12-09 Mitsubishi Heavy Industries, Ltd. Carbon dioxide recovery apparatus and method

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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