GB1031047A - - Google Patents

Info

Publication number
GB1031047A
GB1031047A GB901863A GB901863A GB1031047A GB 1031047 A GB1031047 A GB 1031047A GB 901863 A GB901863 A GB 901863A GB 901863 A GB901863 A GB 901863A GB 1031047 A GB1031047 A GB 1031047A
Authority
GB
United Kingdom
Prior art keywords
acid
thermal treatment
urea
ammonia
raw
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
GB901863A
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.)
Office National Industriel de lAzote
Original Assignee
Office National Industriel de lAzote
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 Office National Industriel de lAzote filed Critical Office National Industriel de lAzote
Publication of GB1031047A publication Critical patent/GB1031047A/en
Expired legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<PICT:1031047/C1/1> Cyanuric acid is made by a process comprising subjecting urea at a temperature of 170 DEG C. or below to a thermal treatment at temperatures between 220 DEG and 340 DEG C. to obtain raw cyanuric acid, and treating the raw acid by acid hydrolysis under pressure to hydrolyse amino derivatives formed during the thermal treatment. The ammonia evolved is recovered by absorption in the mother liquor from the acid hydrolysis and vaporized unreacted urea is recycled. In the embodiment described in relation to the drawing, urea is heated in vessel 1, fed into malaxators 3, then into (optional) finishing screw 10, the inner walls of the malaxators and the finishing screw being maintained at between 220 DEG and 340 DEG C. The raw cyanuric acid is poured into cooled screw exchanger 14, then fed to grinder 15, into aqueous acid in tank 18, into autoclave 24 for the hydrolysis step, and to filtering device 31 for separation of the pure cyanuric acid. The mother liquors pass to saturator 35 to absorb ammonia from the thermal treatment zones, then may be neutralized with more ammonia to recover the ammonium salt of the acid, for example nitric or phosphoric acid used in the hydrolysis step.
GB901863A 1962-03-06 1963-03-06 Expired GB1031047A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR31004777 1962-03-06

Publications (1)

Publication Number Publication Date
GB1031047A true GB1031047A (en) 1966-05-25

Family

ID=9691892

Family Applications (1)

Application Number Title Priority Date Filing Date
GB901863A Expired GB1031047A (en) 1962-03-06 1963-03-06

Country Status (5)

Country Link
BE (1) BE629199A (en)
CH (1) CH413849A (en)
DE (1) DE1470140A1 (en)
GB (1) GB1031047A (en)
LU (1) LU43289A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2035792B1 (en) * 1991-08-21 1993-12-16 Patentes Novedades Sa "INSTALLATION FOR THE OBTAINING OF CYANURIC ACID AND THE CORRESPONDING PROCEDURE"

Also Published As

Publication number Publication date
BE629199A (en) 1963-07-01
CH413849A (en) 1966-05-31
DE1470140A1 (en) 1969-04-17
LU43289A1 (en) 1963-05-02

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