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JPS54120292A - Bromine recovering method - Google Patents

Bromine recovering method

Info

Publication number
JPS54120292A
JPS54120292A JP2731078A JP2731078A JPS54120292A JP S54120292 A JPS54120292 A JP S54120292A JP 2731078 A JP2731078 A JP 2731078A JP 2731078 A JP2731078 A JP 2731078A JP S54120292 A JPS54120292 A JP S54120292A
Authority
JP
Japan
Prior art keywords
soln
effluent
contg
remove
gas
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
JP2731078A
Other languages
Japanese (ja)
Inventor
Kiyoshi Oota
Minoru Ikeda
Hideo Kawasaki
Masaji Nakatani
Tetsuo Kudo
Zenji Nakagawa
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.)
Nissan Engineering Ltd
Nissan Chemical Corp
Original Assignee
Nissan Engineering Ltd
Nissan Chemical Corp
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 Nissan Engineering Ltd, Nissan Chemical Corp filed Critical Nissan Engineering Ltd
Priority to JP2731078A priority Critical patent/JPS54120292A/en
Publication of JPS54120292A publication Critical patent/JPS54120292A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To remove a trace amt. of NH3 from an aq. soln. of a Br cpd. contg. NH3 or NH4 salt in recovery of Br2 from the soln. with Cl2 and steatm, by adding NaOH to the soln. to remove most of NH3 as pretreatment and contacting the pretreated soln. to Cl2, etc. while keeping the soln. at a specific pH value.
CONSTITUTION: An ap. soln. 1 of a Br cpd. contg. 50 g/l of NH3 or NH4 salt and NaOH 2 are introduced into regulation vessel 4, where they are heated to above 60°C with steam 3 at pH 11W13 to release most 5 of NH3. Effluent 6 is fed to stripping tower 8 to strip NH3-contg. gas 10 with stripping gas 9 such as air. Effluent 11 is then introduced into reaction vessel 13 and blown with Cl2 gas 12 to remove a trace amt. of NH3 while keeping effluent 11 at pH≥8. Effluent 15 is fed to acidification vessel 18 to add sulfuric acid 17 and introduced into reaction distilling column 20 for recovering Br2, where it is treated with steam 21 and Cl2 22 to recover Br2 23.
COPYRIGHT: (C)1979,JPO&Japio
JP2731078A 1978-03-10 1978-03-10 Bromine recovering method Pending JPS54120292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2731078A JPS54120292A (en) 1978-03-10 1978-03-10 Bromine recovering method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2731078A JPS54120292A (en) 1978-03-10 1978-03-10 Bromine recovering method

Publications (1)

Publication Number Publication Date
JPS54120292A true JPS54120292A (en) 1979-09-18

Family

ID=12217505

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2731078A Pending JPS54120292A (en) 1978-03-10 1978-03-10 Bromine recovering method

Country Status (1)

Country Link
JP (1) JPS54120292A (en)

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