GB393527A - Process and apparatus for the continuous mutual reaction of liquids - Google Patents

Process and apparatus for the continuous mutual reaction of liquids

Info

Publication number
GB393527A
GB393527A GB1181/33A GB118133A GB393527A GB 393527 A GB393527 A GB 393527A GB 1181/33 A GB1181/33 A GB 1181/33A GB 118133 A GB118133 A GB 118133A GB 393527 A GB393527 A GB 393527A
Authority
GB
United Kingdom
Prior art keywords
vessels
liquid
nitroglycerine
washing
pipe
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
Application number
GB1181/33A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB393527A publication Critical patent/GB393527A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D11/00Solvent extraction
    • B01D11/04Solvent extraction of solutions which are liquid
    • B01D11/0446Juxtaposition of mixers-settlers
    • B01D11/0469Juxtaposition of mixers-settlers with gas agitation

Abstract

In treating a liquid with an immiscible liquid of different p specific gravity, the liquids are caused to flow in opposite directions through a series of mixing vessels without intermediate separation, the vessels being connected by inclined passages or channels in which the lighter liquid flows upwardly and the heavier liquid downwardly. As shown, three mixing vessels A, B, C are provided, each having a pipe l through which air is blown to agitate the liquid; mechanical stirrers may also be <PICT:0393527/IV/1> arranged in the vessels. The vessels are connected by inclined pipes b, c, and inclined overflow pipes a, d are also provided. The operation of the apparatus is described with reference to the washing of nitroglycerine with water or an alkaline solution. The whole apparatus is first filled with washing liquid up to the level of the overflow g, the valve f being closed. Washing liquid is then continuously run in through the pipe w or w<1>, and nitroglycerine through the pipe n or n<1> and the contents of the vessels are agitated. In the pipes a .. d, where no agitating means are present, the nitroglycerine flows downwardly and the washing liquid upwardly, with the result that used washing liquid flows out continuously at g. The valve f is opened when sufficient nitroglycerine has accumulated at s, and the nitroglycerine then withdrawn at e. Water may be supplied to the vessel A and alkali added in the vessel B. Means for heating or cooling the vessels may be provided. The apparatus may be used also for washing other nitroesters or nitro compounds, or for nitrating benzene and other hydrocarbons.ALSO:<PICT:0393527/III/1> In treating a liquid with an immiscible liquid of different specific gravity, the liquids are caused to flow in opposite directions through a series of mixing vessels without intermediate separation, the vessels being connected by inclined passages or channels in which the lighter liquid flows upwardly and the heavier liquid downwardly. As shown, three mixing vessels A, B, C are provided, each having a pipe l through which air is blown to agitate the liquid; mechanical stirrers may also be arranged in the vessels. The vessels are connected by inclined pipes b, c, and inclined overflow pipes a, d are also provided. The operation of the apparatus is described with reference to the washing of nitroglycerine with water or an alkaline solution. The whole apparatus is first filled with washing liquid up to the level of the overflow g, the valve f being closed. Washing liquid is then continuously run in through the pipe w, or w<1> and nitro glycerine through the pipe n or n<1>, and the contents of the vessels are agitated. In the pipes a . . d, where no agitating means are present, the nitroglycerine flows downwardly and the washing liquid upwardly, with the result that used washing liquid flows out continuously at g. The valve f is opened when sufficient notroglycerine has accumulated at s, and the nitroglycerine then withdrawn at e. Water may be supplied to the vessel A and alkali added in the vessel B. Means for heating or cooling the vessels may be provided. The apparatus may be used also for washing other nitroesters or nitro compounds, for nitrating benzene and other hydrocarbons, and for refining petroleum with acids.
GB1181/33A 1932-02-12 1933-01-13 Process and apparatus for the continuous mutual reaction of liquids Expired GB393527A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE393527X 1932-02-12

Publications (1)

Publication Number Publication Date
GB393527A true GB393527A (en) 1933-06-08

Family

ID=6392015

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1181/33A Expired GB393527A (en) 1932-02-12 1933-01-13 Process and apparatus for the continuous mutual reaction of liquids

Country Status (3)

Country Link
US (1) US2048820A (en)
FR (1) FR749002A (en)
GB (1) GB393527A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2645565A (en) * 1950-04-22 1953-07-14 Standard Oil Dev Co Liquid-liquid extraction tower
US2835687A (en) * 1952-03-25 1958-05-20 Glenford H Clewett Isotope fractionation process
US2895808A (en) * 1954-10-19 1959-07-21 Fisons Pest Control Ltd Apparatus for the separation of solutes by partition
US3110568A (en) * 1959-09-07 1963-11-12 Asea Ab Extraction apparatus
US4325888A (en) * 1978-01-13 1982-04-20 Propylox Preparation of peracid by liquid-liquid extraction
FI96968C (en) * 1993-12-02 1996-09-25 Outokumpu Eng Contract Process for extracting metals from large solution streams and apparatus for carrying out the process
CN102276470A (en) * 2010-06-08 2011-12-14 中国石油化工集团公司 Method for nitrifying aromatic hydrocarbon compound by continuous countercurrent

Also Published As

Publication number Publication date
US2048820A (en) 1936-07-28
FR749002A (en) 1933-07-17

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