GB722434A - Process for the production of hexamethylenetetramine - Google Patents

Process for the production of hexamethylenetetramine

Info

Publication number
GB722434A
GB722434A GB4219/52A GB421952A GB722434A GB 722434 A GB722434 A GB 722434A GB 4219/52 A GB4219/52 A GB 4219/52A GB 421952 A GB421952 A GB 421952A GB 722434 A GB722434 A GB 722434A
Authority
GB
United Kingdom
Prior art keywords
solution
hexamethylenetetramine
reaction
ammonia
formaldehyde
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
GB4219/52A
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 GB722434A publication Critical patent/GB722434A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D487/00Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00
    • C07D487/12Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00 in which the condensed system contains three hetero rings
    • C07D487/18Bridged systems

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Hexamethylenetetramine is obtained by reacting ammonia and formaldehyde in solution in a solvent, the reaction being carried out at the boiling-point of the reaction mixture and the heat of reaction that is evolved being utilized as heat for effecting evaporation of the solvent containing the reactants. The heat of reaction is defined as the total heat produced by the absorption and by the solution of the reactants in addition to that of the reaction proper. By selecting suitable pressure conditions, i.e. reduced or increased pressure, with, if required, the addition of another gas, the boiling-point can be fixed as required for the most favourable reaction temperature. Specified solvents are water and alcohol. In carrying out the reaction the reactants may be brought together as follows: (a) formaldehyde is dissolved in water or aqueous alcohol and gaseous ammonia is passed into the solution or otherwise brought into contact with the solution, e.g. in a trickling tower; (b) the ammonia is dissolved in water or aqueous alcohol and gaseous aldehyde is introduced into the ammoniacal solution; (c) gaseous ammonia and gaseous aldehyde are introduced into a solvent such as water or aqueous alcohol or into a solution containing dissolved reaction product; (d) dissolved ammonia and dissolved formaldehyde are interacted. The process can be made continuous by proportioning the formaldehyde and ammonia by means of suitable regulating apparatus, e.g. pH-regulating apparatus, polarographs or conductivity meters. In examples: (1) a 30 per cent aqueous solution of formaldehyde at 20 DEG C. trickles through a trickling tower and meets an ascending current of gaseous ammonia introduced at the bottom. The pressure is adjusted to about 150 mm. of mercury corresponding to a boiling temperature of about 60 DEG C. or to such other pressure as will enable the reaction to be carried out within the preferred temperature range of 50-70 DEG C. The evaporated solvent is condensed and the hexamethylenetetramine formed leaves the column as a 27 per cent aqueous solution which is then evaporated in a vacuum evaporator to form solid hexamethylenetetramine. The ammonia added is proportioned by means of a pH regulating apparatus to a neutral outflowing solution; (2) a 27 per cent solution of hexamethylenetetramine is prepared as in (1) and is evaporated down to give a concentrated solution into which gaseous ammonia is introduced whereby the solubility of the hexamethylenetetramine is lowered and pure hexamethylenetetramine is precipitated and separated from the ammoniacal mother liquor which is again reacted with a 30 per cent formaldehyde solution at a pressure of 156 mm. of mercury, corresponding to a boiling temperature of 61 DEG C. whereby the ammonia dissolved in the mother liquor is converted into hexamethylenetetramine. The outgoing vapours are condensed and the solution of hexamethylenetetramine flowing out of the reaction apparatus is again introduced to yield a further quantity of hexamethylenetetramine.
GB4219/52A 1951-02-19 1952-02-18 Process for the production of hexamethylenetetramine Expired GB722434A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE722434X 1951-02-19

Publications (1)

Publication Number Publication Date
GB722434A true GB722434A (en) 1955-01-26

Family

ID=6631242

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4219/52A Expired GB722434A (en) 1951-02-19 1952-02-18 Process for the production of hexamethylenetetramine

Country Status (1)

Country Link
GB (1) GB722434A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0712839A1 (en) * 1994-11-18 1996-05-22 Norsk Hydro A/S Process for the preparation of urea

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0712839A1 (en) * 1994-11-18 1996-05-22 Norsk Hydro A/S Process for the preparation of urea
US5686647A (en) * 1994-11-18 1997-11-11 Norsk Hydro A.S Process for the preparation of urea

Similar Documents

Publication Publication Date Title
US2593001A (en) Process for manufacture of a diphenyl sulfone
GB722434A (en) Process for the production of hexamethylenetetramine
US1480166A (en) Manufacture of hydrazine
GB952746A (en) Improvements in or relating to the manufacture of dinitrogen tetroxide
US3932504A (en) Urea manufacture
US3034861A (en) Process for preparing hydrazine
US2050442A (en) Manufacture of ethyl alcohol
US3277179A (en) Manufacture of aqueous formaldehyde solution and paraformaldehyde
US2992896A (en) Preparation of carbonyl sulfide
US2275825A (en) Manufacture of hydrochloric acid
US2762800A (en) Manufacture of hexamethylene-
US2529887A (en) Process for the preparation of anisole
US2243484A (en) Process for the preparation of monohalogenated ketones
US1733721A (en) Carnie b
US3203756A (en) Method of preparing permonosulphates
US3211788A (en) Biuret control in urea process
US2108011A (en) Preparation of ethylene bromide
US2067899A (en) Manufacture of ammonium sulphate
US2759978A (en) Production of chloral
US2739037A (en) Process for production of ammonium nitrate
US3167387A (en) Process for the production of alkaline cyanates in sulfoxide and sulfone solvents
US4026999A (en) Production of iron (II) chloride and chlorine from ferric chloride
US4283577A (en) Method for making ethylene chlorohydrin
US2856430A (en) Method for preparing monohaloacetones
US2675298A (en) Hydrazine manufacture