Patent GB-838001-A (GB)
Title: Improvements in or relating to processes for the recovery of ammonia from coke oven gas
IPC: C05B7/00
Filed: 1958-02-03
Abstract: <PICT:0838001/III/1> Ammonia is removed from coke oven gases by a process which comprises contacting the gases with a first solution saturated with respect to diammonium phosphate and which is incapable of absorbing all of the ammonia present and which contains sufficient phosphoric acid to maintain it at a pH of 6.5-7 thereby to form diammonium phosphate from the ammonia absorbed, removing entrained liquid from the residual gas and thereafter contacting it with a second solution saturated with respect to ammonium sulphate and containing 2-8% wt. of H2SO4 thereby to effect absorption of the remaining ammonia as ammonium sulphate. Coke oven gases are supplied to inlet 23 of saturator P being the first of two identical separators P and S connected by a conduit C, and flow through annular absorption zone X where they are washed with a saturated solution of diammonium phosphate, the pH of which is maintained at 6.5-7 to prevent formation of monoammonium phosphate, which is sprayed into the chamber by nozzles 31 uniformly distributed over the upper portion 25 of the absorption zone, whereby the major portion of the ammonia is absorbed forming a supersaturated solution of diammonium phosphate, which collects in bath 43 and is discharged therefrom by 45 through 51 into crystallizer bowl 30.  Whilst a large amount of liquor is discharged through 51, some exits through openings 53 and is caused to flow upwards adjacent 45 by deflectors 55 thereby ensuring that the general flow of liquid in the bowl 30 is in an upward direction.  The super saturation of the liquor discharged from 45 is released by contact with crystals of diammonium phosphate held in suspension in 30 upon which the excess diammonium phosphate is deposited, the crystals growing in size until they settle into the lower portion of crystallizer 30 to be removed by suction heads 70 which deliver to a conventional centrifuge and drying apparatus (not shown).  Residual mother liquor which consists of a saturated solution of diammonium phosphate is recycled from the top of 30 to spray heads 31 through 49 by means of pump 46.  Coke-oven gases containing a reduced proportion of ammonia leave absorption chamber X by riser 29 and are discharged tangentially into chamber 7, between member 27 and pipe 28, by horizontal passage 33.  The gases gyrate about 28 thereby throwing any liquid entrained therein against wall 27 such liquid draining into 43, whilst the gases descend chamber Y and thence flow through 28 into conduit C.  An overflow 73 maintains the level of liquid in 43 such that chamber 7 is sealed from the absorption zone X, and is in direct communication with a tar skimmer tank 77, the supernatant liquid from which is conveyed to storage tank 81 and by way of pump 83 to spray unit 85.  Fresh phosphoric acid is added from tank 79 in such quantity as is required to maintain the pH of the liquor in the system at 6.5-7. Coke-oven gases containing residual ammonia pass through C to a second separator S identical in design and operation to separator P except that gases are now washed with a saturated solution of ammonium sulphate with the subsequent formation of ammonium sulphate crystals which are isolated, the sulphuric acid content of the washing liquor being maintained at 2-8% by wt. by fresh additions of acid from tank 791. Crystals of diammonium phosphate and ammonium sulphate may, after drying, be blended to provide a fertilizer having a desired nitrogen content. Specification 669,425 is referred to.