JPH0295501U - - Google Patents

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Publication number
JPH0295501U
JPH0295501U JP232789U JP232789U JPH0295501U JP H0295501 U JPH0295501 U JP H0295501U JP 232789 U JP232789 U JP 232789U JP 232789 U JP232789 U JP 232789U JP H0295501 U JPH0295501 U JP H0295501U
Authority
JP
Japan
Prior art keywords
section
liquid
column
recovery
concentration
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
Application number
JP232789U
Other languages
Japanese (ja)
Other versions
JPH0634801Y2 (en
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 filed Critical
Priority to JP232789U priority Critical patent/JPH0634801Y2/en
Publication of JPH0295501U publication Critical patent/JPH0295501U/ja
Application granted granted Critical
Publication of JPH0634801Y2 publication Critical patent/JPH0634801Y2/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)

Description

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

第1図は本考案の実施例にかかる蒸留装置の基
本構成図、第2図は本考案の第1実施例にかかる
熱交換構造を示す蒸留塔の一部拡大断面図、第3
図は第2図―線断面図、第4図は第2図の一
部拡大図、第5図は本考案の第2実施例にかかる
熱交換構造を示す第2図相当図、第6図は内部熱
交換方式をとる蒸留装置のシステム原理図である
。 1…濃縮部、2…回収部、11…伝熱壁となる
濃縮部の周壁、12,22…棚段、5…加圧管路
、51…加圧手段としての圧縮機、6…減圧管路
、61…減圧手段としての減圧弁、7…液ガイド
部、73…同ガイド部の流下部、74…同溢流部
、9…蒸気ガイド板(蒸気ガイド部材)。
FIG. 1 is a basic configuration diagram of a distillation apparatus according to an embodiment of the present invention, FIG. 2 is a partially enlarged sectional view of a distillation column showing a heat exchange structure according to a first embodiment of the present invention, and FIG.
The figure is a cross-sectional view taken along the line shown in FIG. 2, FIG. 4 is a partially enlarged view of FIG. 2, FIG. 5 is a view equivalent to FIG. 1 is a system principle diagram of a distillation apparatus that uses an internal heat exchange method. DESCRIPTION OF SYMBOLS 1... Concentrating section, 2... Recovery section, 11... Peripheral wall of the concentrating section serving as a heat transfer wall, 12, 22... Shelf, 5... Pressurizing pipe line, 51... Compressor as pressurizing means, 6... Depressurizing pipe line , 61...Pressure reducing valve as a pressure reducing means, 7...Liquid guide section, 73...Downstream part of the same guide part, 74...Same overflow part, 9...Steam guide plate (steam guide member).

Claims (1)

【実用新案登録請求の範囲】 1 蒸留塔の回収部と濃縮部がそれぞれ互いに独
立した棚段塔に構成され、回収部と濃縮部との間
に、回収部の塔頂部から出る蒸気を加圧して濃縮
部の塔底部に送り込む加圧手段を備えた加圧管路
と、濃縮部の塔底部の液を減圧して回収部の塔頂
部に戻す減圧手段を備えた減圧管路とが設けられ
、これら濃縮部と回収部との間で熱交換作用が行
なわれるように構成された蒸留装置において、上
記回収部と濃縮部が、いずれか一方が内塔、他方
が外塔となるように同心配置されて、濃縮部と回
収部が伝熱壁を介して接する二重塔構造の蒸留塔
が構成され、かつ、上記回収部内に、棚段上の液
を下の棚段に導く液ガイド部が設けられ、この液
ガイド部は、液を上記伝熱壁に沿つて流下させる
流下部と、この流下部の下端から立上がつて液を
溢流させる溢流部とからなることを特徴とする蒸
留装置。 2 濃縮部内に、濃縮部内蒸気を伝熱壁に向けて
ガイドする蒸気ガイド部材が設けられたことを特
徴とする請求項1記載の蒸留装置。
[Claims for Utility Model Registration] 1. The recovery section and concentration section of a distillation column are each configured as a tray column independent of each other, and between the recovery section and concentration section, the steam emitted from the top of the column of the recovery section is pressurized. A pressurizing pipe is provided with a pressurizing means for feeding the liquid into the bottom of the concentrating section, and a reducing pipe is equipped with a reducing means to reduce the pressure of the liquid at the bottom of the concentrating section and return it to the top of the recovery section. In a distillation apparatus configured to perform heat exchange between the concentration section and the recovery section, the recovery section and the concentration section are arranged concentrically so that one is an inner column and the other is an outer column. A distillation column with a double column structure is constructed in which the concentration section and the recovery section are in contact with each other via a heat transfer wall, and a liquid guide section is provided in the recovery section to guide the liquid on the tray to the tray below. The liquid guide section is characterized by comprising a flow section that allows the liquid to flow down along the heat transfer wall, and an overflow section that rises from the lower end of the flow section and causes the liquid to overflow. Distillation equipment. 2. The distillation apparatus according to claim 1, further comprising a steam guide member provided in the concentrating section to guide the vapor in the concentrating section toward a heat transfer wall.
JP232789U 1989-01-12 1989-01-12 Distillation equipment Expired - Fee Related JPH0634801Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP232789U JPH0634801Y2 (en) 1989-01-12 1989-01-12 Distillation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP232789U JPH0634801Y2 (en) 1989-01-12 1989-01-12 Distillation equipment

Publications (2)

Publication Number Publication Date
JPH0295501U true JPH0295501U (en) 1990-07-30
JPH0634801Y2 JPH0634801Y2 (en) 1994-09-14

Family

ID=31202998

Family Applications (1)

Application Number Title Priority Date Filing Date
JP232789U Expired - Fee Related JPH0634801Y2 (en) 1989-01-12 1989-01-12 Distillation equipment

Country Status (1)

Country Link
JP (1) JPH0634801Y2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0866601A (en) * 1994-08-29 1996-03-12 Kimura Chem Plants Co Ltd Inner heat exchange type distillation column
WO2006022208A1 (en) * 2004-08-24 2006-03-02 Kansai Chemical Engineering Co., Ltd. Multi-structure internal heat exchange type distillation tower
CN111500306A (en) * 2020-06-01 2020-08-07 河南孟飞实业有限公司 Double-layer rectifying tower for preparing light white oil

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0866601A (en) * 1994-08-29 1996-03-12 Kimura Chem Plants Co Ltd Inner heat exchange type distillation column
WO2006022208A1 (en) * 2004-08-24 2006-03-02 Kansai Chemical Engineering Co., Ltd. Multi-structure internal heat exchange type distillation tower
JPWO2006022208A1 (en) * 2004-08-24 2008-05-08 関西化学機械製作株式会社 Multi-structure internal heat exchange distillation column
CN111500306A (en) * 2020-06-01 2020-08-07 河南孟飞实业有限公司 Double-layer rectifying tower for preparing light white oil
CN111500306B (en) * 2020-06-01 2024-04-12 河南孟飞实业有限公司 Double-layer rectifying tower for preparing light white oil

Also Published As

Publication number Publication date
JPH0634801Y2 (en) 1994-09-14

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Legal Events

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LAPS Cancellation because of no payment of annual fees