JP2001025601A5 - - Google Patents

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Publication number
JP2001025601A5
JP2001025601A5 JP1999198316A JP19831699A JP2001025601A5 JP 2001025601 A5 JP2001025601 A5 JP 2001025601A5 JP 1999198316 A JP1999198316 A JP 1999198316A JP 19831699 A JP19831699 A JP 19831699A JP 2001025601 A5 JP2001025601 A5 JP 2001025601A5
Authority
JP
Japan
Prior art keywords
dropping
pipe
supplied
ethanol
needle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP1999198316A
Other languages
Japanese (ja)
Other versions
JP2001025601A (en
Filing date
Publication date
Application filed filed Critical
Priority to JP11198316A priority Critical patent/JP2001025601A/en
Priority claimed from JP11198316A external-priority patent/JP2001025601A/en
Publication of JP2001025601A publication Critical patent/JP2001025601A/en
Publication of JP2001025601A5 publication Critical patent/JP2001025601A5/ja
Pending legal-status Critical Current

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Description

図示例において、滴下針28は、管(主管14および枝管16)の滴下口26に対向する頂部に固定(螺合)されるボルト30の下端(液導入24では、ストレーナの下端)に固定され、此処から垂下するようにして滴下口26を通過、突出するが、本発明において、滴下針28の取り付け方法は、これに限定はされず、例えば、管の内壁頂部に溶接等で直接滴下針28を固定する方法等、公知の方法が各種利用可能である。 In the illustrated example, the dropping needle 28 is attached to the lower end of the bolt 30 fixed (screwed) to the top of the pipe (main pipe 14 and branch pipe 16) facing the dropping port 26 (in the liquid introduction portion 24, the lower end of the strainer). It is fixed and passes through and protrudes from the dropping port 26 so as to hang down from here, but in the present invention, the method of attaching the dropping needle 28 is not limited to this, and for example, it is directly attached to the top of the inner wall of the pipe by welding or the like. Various known methods such as a method of fixing the dropping needle 28 can be used.

このような液分散器10の液導入部24に、定量ポンプでエタノール(10℃での粘度が約1.3cp)を30L(リットル)/hrおよび60L/hr供給して、充填塔内にエタノールを分散供給した。各例における流量は、30L/hrの場合が、
(0.03[m3 /hr])/(0.283[m2 ])
≒0.11[m3 /(m2 ・hr)]
60L/hrの場合が、
(0.06[m3 /hr])/(0.283[m2 ])
≒0.21[m3 /(m2 ・hr)]
である。
Ethanol (viscosity at 10 ° C. of about 1.3 cp) is supplied at 30 L (liter) / hr and 60 L / hr to the liquid introduction section 24 of the liquid disperser 10 by a metering pump, and ethanol is supplied into the filling column. Was distributed and supplied. When the flow rate in each example is 30 L / hr,
(0.03 [m 3 / hr]) / (0.283 [m 2])
≒ 0.11 [m 3 / (m 2 · hr)]
In the case of 60L / hr,
(0.06 [m 3 / hr]) / (0.283 [m 2])
≒ 0.21 [m 3 / (m 2 · hr)]
Is.

JP11198316A 1999-07-13 1999-07-13 Liquid disperser Pending JP2001025601A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11198316A JP2001025601A (en) 1999-07-13 1999-07-13 Liquid disperser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11198316A JP2001025601A (en) 1999-07-13 1999-07-13 Liquid disperser

Publications (2)

Publication Number Publication Date
JP2001025601A JP2001025601A (en) 2001-01-30
JP2001025601A5 true JP2001025601A5 (en) 2006-04-27

Family

ID=16389105

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11198316A Pending JP2001025601A (en) 1999-07-13 1999-07-13 Liquid disperser

Country Status (1)

Country Link
JP (1) JP2001025601A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100463471B1 (en) * 2001-11-20 2004-12-30 (주)에이엠티퍼시픽 The Device and Method of liquid distribution
CN103386210B (en) * 2012-05-08 2015-01-21 中国石油化工集团公司 Inner sleeve plate structure of packed fractionating tower
KR101745076B1 (en) * 2015-03-31 2017-06-08 고려대학교 산학협력단 Bubble diffuser

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