GB1099856A - Granulation process and apparatus - Google Patents

Granulation process and apparatus

Info

Publication number
GB1099856A
GB1099856A GB2527265A GB2527265A GB1099856A GB 1099856 A GB1099856 A GB 1099856A GB 2527265 A GB2527265 A GB 2527265A GB 2527265 A GB2527265 A GB 2527265A GB 1099856 A GB1099856 A GB 1099856A
Authority
GB
United Kingdom
Prior art keywords
drum
urea
ammonium nitrate
supplied
zone
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
GB2527265A
Inventor
Joshua Beaumont Thompson
Gordon Charles Hildred
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.)
Teck Metals Ltd
Original Assignee
Teck Metals 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
Priority to US329127A priority Critical patent/US3398191A/en
Application filed by Teck Metals Ltd filed Critical Teck Metals Ltd
Priority to GB2527265A priority patent/GB1099856A/en
Publication of GB1099856A publication Critical patent/GB1099856A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/16Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/12Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic in rotating drums
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C1/00Ammonium nitrate fertilisers
    • C05C1/02Granulation; Pelletisation; Stabilisation; Colouring

Abstract

Nitrogenous fertilizer compounds, e.g. ammonium nitrate or urea, are produced in granular form by apparatus comprising a drum 10 which rests on rollers 11 and is separated b a ring 15, of adjustable width, into a granulating zone A of between one half and the full length of a cooling zone B and which is inclined at 1-3 degrees to the horizontal and is rotated, by gear engagement with ring 14, at between 4 and 12 r.p.m whereby solid particles of fertlizer, supplied through pipe 20, are advanced in a bed through zones A and B whilst being raised therefrom by lifting elements (22) Figs. 3 and 4, not shown) to form a continuous cascading curtain <PICT:1099856/C1/1> which, in zone A, is sprayed via pipe 21 with an anhydrous nitrogenous melt of at least 98% and preferably 99 to 99.5%, ammonium nitrate or urea, at 5 DEG to 25 DEG C., and preferably 10 DEG C., above its crystallization teperature whilst cooling air, supplied at outlet 31, is exhausted through duct 23 and is always at least 60 DEG C. below the temperature of the molten spray. The ammonium nitrate or urea is automatically formed in a reactor (40) (Fig.1, not shown) as an aqueous solution which is concentrated in an evaporator (41) and supplied to the drum (10) along a heated pipe line (21). Granules discharged from the drum (10) are screened in a unit (43) with correct sized material passing via a cooler (42), to a unit for coating, e.g. with diatomite, oversize material passing for incorporating into the solution and for recirculation via a cursher (45) and undersize material, together with material collected at a drum inlet hopper (46) being fed back to the drum inlet pipe (20). Fines are collected from the drum cooling air exhaust 23 and the exhaust from the cooler 42 in a separator (44) and returned for concentration in the evaporator (41). Ammonium nitrate and urea granules are produced predominantly in the size range of 0.131 to 0.065 inch diameter, the nitrate having a bulk density greater then 50 lb./cubic feet and both the nitrates and urea granules being characterized by their hardness.ALSO:Nitrogenous fertilizer compounds, e.g. ammonium nitrate or urea, are produced in granular form by apparatus comprising a drum 10 which rests on rollers 11 and is separated by a ring 15, of adjustable width, into a granulating zone A of between one half and the full length of a cooling zone B and which is inclined at 1-3 degrees to the horizontal and is rotated, by gear engagement with ring 14, at between 4 and 12 r.p.m., whereby solid particles of fertilizer, supplied through pipe 20, are advanced in a bed through zones A and B whilst being raised therefrom by lifting elements (22) (Figs. 3 and 4, not shown) to form a continuous cascading curtain which, in zone A, is sprayed via pipe 21 with an anhydrous nitrogenous melt of at least 98%, and preferably 99 to 99.5%, ammonium nitrate or urea at 5 DEG to 25 DEG C., and preferably 10 DEG C., above its crystallization temperature whilst cooling air, supplied at outlet 31, is exhausted through duct 23 and is always at least 60 DEG C. below the temperature of the molten spray. The ammonium nitrate or urea is automatically formed in a reactor (40) (Fig. 1, not shown) as an aqueous solution which is concentrated in an evaporator (41) and supplied to the drum <PICT:1099856/C2/1> (10) along a heated pipe line (21). Granules discharged from the drum (10) are screened in a unit (43) with correct sized material passing, via a cooler (42), to a unit for coating e.g. with diatomite, oversize material passing for incorporating into the solution and for recirculation via a crusher (45) and undersize material, together with material collected at a drum inlet hopper (46), being fed back to the drum inlet pipe (20). Fines are collected from the drum cooling air exhaust 23 and the exhaust from the cooler 42 in a separator 44 and returned for concentration in the evaporator (41). Ammonium nitrate and urea granules are produced predominantly in the size range of 0.131 to 0.065 inch diameters, the nitrate having a bulk density greater than 50 lb./cubic feet and both the nitrates and urea granules being characterized by their hardness.
GB2527265A 1963-12-09 1965-06-15 Granulation process and apparatus Expired GB1099856A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US329127A US3398191A (en) 1963-12-09 1963-12-09 Process for the production of granular nitrogenous compounds
GB2527265A GB1099856A (en) 1965-06-15 1965-06-15 Granulation process and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2527265A GB1099856A (en) 1965-06-15 1965-06-15 Granulation process and apparatus

Publications (1)

Publication Number Publication Date
GB1099856A true GB1099856A (en) 1968-01-17

Family

ID=10225030

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2527265A Expired GB1099856A (en) 1963-12-09 1965-06-15 Granulation process and apparatus

Country Status (1)

Country Link
GB (1) GB1099856A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1542388B1 (en) * 1965-12-14 1971-05-13 Potasse & Engrais Chimiques Process for the granulation of substances present in the form of a melt, suspension or solution
WO2016179718A1 (en) * 2015-05-13 2016-11-17 K+S Chile S.A. Agglomeration drum for pre-treating minerals

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1542388B1 (en) * 1965-12-14 1971-05-13 Potasse & Engrais Chimiques Process for the granulation of substances present in the form of a melt, suspension or solution
WO2016179718A1 (en) * 2015-05-13 2016-11-17 K+S Chile S.A. Agglomeration drum for pre-treating minerals
US10544480B2 (en) 2015-05-13 2020-01-28 K+S Chile S.A. Agglomeration drum for pre-treating minerals

Similar Documents

Publication Publication Date Title
US4353730A (en) Granulating process
US4842790A (en) Method and apparatus for producing high-strength grannular particulates from low-strength prills
GB962265A (en) Improvements in the granulating and drying of fluid materials such as aqueous solutions, pastes and slurries
NO160956B (en) SYNKRON SUPPRESSION SCRAMBLING OF TELEVISION SIGNALS FOR SUBSCRIPTION TV AND PROGRESS MEASURES BY SYNKRON SUPPRESSION SCRAMBLER SUBSCRIPTION TV SYSTEM.
US6132484A (en) Wet granulation method for generating fertilizer granules
GB1124780A (en) Process and apparatus for obtaining a solid product from melts, solutions, slurries and the like
US6454979B1 (en) Wet granulation method for generating granules
US6331193B1 (en) Wet granulation method generating sulfur granules
US3825414A (en) Urea-ammonium polyphosphate production
US6805821B2 (en) Wet granulation method for generating granules
US3398191A (en) Process for the production of granular nitrogenous compounds
GB1099856A (en) Granulation process and apparatus
US3085870A (en) Granular materials
US3585043A (en) Method for preparing a homogenous silage additive
US4564505A (en) Process and apparatus for simultaneous material granulation and classification
US3299132A (en) Process for granulating urea
GB1119078A (en) Method and apparatus for obtaining solid products in granulated form
US3258849A (en) Rotary granulator and dryer
GB1448031A (en) Method of granulating powdery material in particular urea
GB989761A (en) Granulators
GB1098593A (en) Fertilizers
ES2058371T3 (en) PROCEDURE TO REPRESS THE FORMATION OF POWDER AND FINAL GRAIN DURING THE AMMONIUM NITRATE GRANULATION.
SU1153971A1 (en) Method of obtaining granulated complex fertilizers
GB1412487A (en) Manufacture of granular fertilizers
ES366856A1 (en) Process for mixed fertilizer granulation