GB877906A - A process for the manufacture of cyanuric chloride - Google Patents

A process for the manufacture of cyanuric chloride

Info

Publication number
GB877906A
GB877906A GB1392758A GB1392758A GB877906A GB 877906 A GB877906 A GB 877906A GB 1392758 A GB1392758 A GB 1392758A GB 1392758 A GB1392758 A GB 1392758A GB 877906 A GB877906 A GB 877906A
Authority
GB
United Kingdom
Prior art keywords
less
activated carbon
gas
cyanuric chloride
chloride
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
GB1392758A
Inventor
Toshio Niwa
Masao Yoshizawa
Akira Nakatsuchi
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.)
ZH NITTO RIKAGAKU KENKYUSHO
Nitto Chemical Industry Co Ltd
Original Assignee
ZH NITTO RIKAGAKU KENKYUSHO
Nitto Chemical Industry 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 ZH NITTO RIKAGAKU KENKYUSHO, Nitto Chemical Industry Co Ltd filed Critical ZH NITTO RIKAGAKU KENKYUSHO
Priority to GB1392758A priority Critical patent/GB877906A/en
Publication of GB877906A publication Critical patent/GB877906A/en
Expired legal-status Critical Current

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Abstract

Cyanuric chloride is prepared by passing hydrogen cyanide gas having a water content of less than 0.5% and chlorine gas through a bed of activated carbon catalyst at a raised temperature. The reaction is effected with a mol ratio Cl2:HCN 1.00 to 1.10, at 300-450 DEG C., and space velocity 40-120 hr. The product is condensed from the effluent and any cyanogen chloride in the product gas is recycled to the process. The gases are dried to less than 0.5% water content by calcium chloride, or silica gel. The activated carbon may be prepared by treating a carbonized organic substance at above 800 DEG C. with a stream of water vapour, carbon monoxide, or carbon dioxide, or by heating the substance with metallic chlorides, e.g. ZnCl2. The activated carbon should be dehydrated by heating at 700-1000 DEG C. under vacuum, e.g. less than 50 mm. Hg., or in an inert gas, e.g. CO2 or N2, cooled, and then saturated with cyanuric chloride at 200-300 DEG C. The resulting carbon catalyst of 3-10 mesh is filled into a tower.
GB1392758A 1958-05-01 1958-05-01 A process for the manufacture of cyanuric chloride Expired GB877906A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1392758A GB877906A (en) 1958-05-01 1958-05-01 A process for the manufacture of cyanuric chloride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1392758A GB877906A (en) 1958-05-01 1958-05-01 A process for the manufacture of cyanuric chloride

Publications (1)

Publication Number Publication Date
GB877906A true GB877906A (en) 1961-09-20

Family

ID=10031917

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1392758A Expired GB877906A (en) 1958-05-01 1958-05-01 A process for the manufacture of cyanuric chloride

Country Status (1)

Country Link
GB (1) GB877906A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997002091A1 (en) * 1995-07-05 1997-01-23 Dsm N.V. Supported carbonylation catalyst

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997002091A1 (en) * 1995-07-05 1997-01-23 Dsm N.V. Supported carbonylation catalyst

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