PL45932B1 - - Google Patents

Download PDF

Info

Publication number
PL45932B1
PL45932B1 PL45932A PL4593262A PL45932B1 PL 45932 B1 PL45932 B1 PL 45932B1 PL 45932 A PL45932 A PL 45932A PL 4593262 A PL4593262 A PL 4593262A PL 45932 B1 PL45932 B1 PL 45932B1
Authority
PL
Poland
Prior art keywords
ammonium nitrate
gypsum
calcium
ammonium
nitrate
Prior art date
Application number
PL45932A
Other languages
Polish (pl)
Filing date
Publication date
Application filed filed Critical
Publication of PL45932B1 publication Critical patent/PL45932B1/pl

Links

Description

2 OpuMlkawajjp dnia Z9 maja 1962 r.Mb <& § siBLlOTEK, £ ^ POLSKIEJ RZECZYPOSPOLITEJ LUDOWEJ OPIS PATENTOWY Nr 45932 Ki. 16, 6 Zaklady Azotowe „Kedzierzyn" *) Kedzierzyn, Polska Sposób zmniejszenia rozkladu azotanu amonowego zawartego w saletrzaku Patent trwa od dnia 12 marca 1962 r.Saletrzak produkuje sie przez mechaniczne zmieszanie drobno zmielonego wapniaka ze ste¬ zonym roztworem azotanu amonowego w tem¬ peraturze okolo 145—150°C. W procesie miesza¬ nia jak tez w dalszych etapach procesu pro¬ dukcji saletrzaku i w czasie skladowania za¬ chodza niepozadane reakcje chemiczne, w wy¬ niku których ulatnia sie amoniak, powodujac straty azotu.Stwierdzono, ze dodatek malych ilosci siar¬ czanu wapnia lub siarczanu amonu obniza sto¬ pien rozkladu azotanu amonowego w procesie produkcji saletrzaiku.Wplyw dodatku tych soli na stopien rozkladu saletrzaku badano w warunkach laboratoryj¬ nych. Otrzymane wyniki przedstawiono w ta¬ blicy.I-Q Nr pró 1 1 2 3 4 5 6 7 1 8 Ilosc i rodzaj dodatków bez dodatków »» „ !# ,» ii ti 0,1# CaS04 Vi H, 0*) 0,5$ CaS04 Vi H2 O 0,2# CaS04 Vi H, O 0,5X (NH4)2 S04 cd 53 5T 2g 154 154 154 154 154 1 154 154 154 Ir? 1,56 1,57 1,5 1,621 0,63 0,54 0,54 0,62 Charaklerp- atpka stopu 1 i 73 a O ° 24,01 - - - 25,6 - - o ** 1 X ** 1 0,95 ¦ -. J 0,971 - 1 0,451 - 1 - 1 - I-I •) Wlasciciel patentu oswiadczyl, ze wspól¬ twórcami wynalazku sa Hubert Zajcmz, Stani¬ slaw Kocierz, Edward Jankowiak i Henryk Maciejec.*) Procentowa zawartosc siarczanów obliczono w stosunku do lacznej masy azotanu, maczki wapiennej oraz wody /stopu saletrzakowego.Próby z dodatkiem gipsu i siaiczanu amonu powtórzono w skali przemyslowej. Potwier¬ dzily one wyniki uzyskane w Laboratorium.W mieszalnikach w których odbywa sie pro¬ ces mieszania maczki wapiennej ze stezonymroztworem azotanu amonu wydziela sie znaczna ilosc amoniaku.Po dodaniu do stopu gipsu lub siarczanu amonu, ilosci wydzielajacego sie amoniaku byly znacznie mniejsze.Pomiar ilosci tego amoniaku jest trudny i niedokladny w skali technicznej. Ilosci jego a tym samym straty azotu mozna stwierdzic* metoda posrednia przez oznaczenie Ca^NO^h w produkcie koncowym, który powstaje w wy¬ niku rozkladu azotanu amonowego.| Nr j próbg 1 2 3 4 /aumriosc gipsom stopie saletrzekotrjm •/• 0,19 0,21 slady 0' Zawartosc 1 1 Ca/NOa/2 uj stopie % \ 0,57 0,56 0,93 1,12 Wedlug wynalazku w warunkach przemyslo¬ wych, gips dodaje sie do kamienia wapienne¬ go na itasmie transportowej kamienia z haldy do lamaczy, przy czym wprowadza sie okolo 0,1%—3,0% gipsu w stosunku do masy kamie¬ nia.Wymieszanie gipsu z wapniakiem odbywa sie w lamaczu, bunkrze nad mlynem, w mlynie w urzadzeniach transportowych i wreszcie w samym mieszalniku. Obliczenie ilosci po¬ trzebnego gipsu w stosunku do transportowa¬ nego kamienia jest proste, gdyz natezenie prze¬ plywu kamienia na transporterze nie ulega wa¬ haniom. W przypadku zastapienia gipsu siar¬ czanem amonowym, ten ostatni wprowadza sie w ilosci 0,1—2% w stosunku do masy saletrza- ku, do roztworu azotanu amonowego przed lub po jego odparowaniu a nastepnie miesza ze zmielonym wapniakiem. 948, ESW „Prasa", Kielce, Dodatek siarczanu wapnia lub amonu do stopu saletrzaku podwyzsza jego temperature krzepniecia w stosunku do stopu saletrzako- wego bez tych dodatków. Zjawisko to odgrywa wazna role w procesie granulacji, powodujac calkowite skrzepniecie granulki przed osiagnie¬ ciem dna wiezy. Granulka saletrzaku bez do¬ datku wymienionych soli osiagajac dno wiezy jest plastyczna i zlepia sie z innymi tworzac duze aglomeraty, a ponad to podczas dalszej obróbki saletrzaku to jest chlodzenia, lamania i sortowania, daje duzo podziarna, które zale¬ pia sita, stwarza trudnosci przy przerobie pylu oraz pogarsza wlasciwosci produktu w czasie jego magazynowania. Postepujac sposobem we¬ dlug wynalazku niedogodnosci te zostaja wy¬ eliminowane, przy czym otrzymuje sie produkt stosunkowo malo hygroskopijny, z powodu zmniejszonej zawartosci azotanu wapnia, oraz malo podatny na zbrylanie. PL2 OpuMlkawajjp on May 9, 1962 Mb <& § siBLLOTEK, £ ^ POLISH PEOPLE'S REPUBLIC PATENT DESCRIPTION No. 45932 Ki. 16, 6 Zakład Azotowe "Kedzierzyn" *) Kedzierzyn, Poland Method of reducing the decomposition of ammonium nitrate contained in calcium ammonium nitrate The patent was valid from March 12, 1962 Saletrzak is produced by mechanically mixing finely ground limestone with a steep solution of ammonium nitrate at temperature around 145-150 ° C. In the mixing process, as well as in the further stages of the nitro-chalk production process, and during storage, undesirable chemical reactions take place, as a result of which ammonia is released, causing nitrogen loss. the amount of calcium sulphate or ammonium sulphate lowers the decomposition rate of ammonium nitrate in the production of nitro-chalk. The effect of the addition of these salts on the degree of decomposition of calcium ammonium nitrate was investigated in laboratory conditions. The obtained results are presented in the table. 4 5 6 7 1 8 Number and type of additives without additives »» "! #,» Ii ti 0.1 # CaS04 Vi H, 0 *) 0.5 $ CaS04 Vi H2 O 0.2 # CaS04 Vi H, O 0 , 5X (NH4) 2 S04 cd 53 5T 2g 154 154 15 4 154 154 1 154 154 154 Ir? 1.56 1.57 1.5 1.621 0.63 0.54 0.54 0.62 Charaklerp- atpka alloy 1 and 73 a O ° 24.01 - - - 25.6 - - o ** 1 X ** 1 0.95 ¦ -. J 0.971 - 1 0.451 - 1 - 1 - II •) The patent owner stated that the authors of the invention are Hubert Zajcmz, Stanisław Kocierz, Edward Jankowiak and Henryk Maciejec. *) The percentage of sulphates was calculated in relation to the total mass of nitrate, lime flour and water / calcium ammonium nitrate alloy. The tests with the addition of gypsum and ammonium sulphate were repeated on an industrial scale. They confirmed the results obtained in the laboratory. In the mixers in which the lime flour was mixed with a concentrated solution of ammonium nitrate, a significant amount of ammonia was released. After adding gypsum or ammonium sulphate to the melt, the amount of ammonia released was much smaller. of this ammonia is difficult and inaccurate on a technical scale. The amount of nitrogen, and thus the loss of nitrogen, can be determined by the indirect method by determining the Ca 2 NO 2 h in the final product, which is formed as a result of the decomposition of ammonium nitrate. No. j sample g 1 2 3 4 / gypsum ammonia, nitrate grade, cross-section • / • 0.19 0.21 traces 0 'Content 1 1 Ca / NOa / 2 cu in% \ 0.57 0.56 0.93 1.12 According to the invention in industrial conditions, gypsum is added to the limestone on the conveyor belt of the halide stone to the breakers, with the addition of about 0.1% to 3.0% gypsum based on the weight of the stone. takes place in the breaker, in the bunker above the mill, in the mill in the transport equipment and finally in the mixer itself. Calculating the amount of gypsum required in relation to the stone transported is simple, since the flow rate of the stone on the conveyor does not vary. In the case of replacing gypsum with ammonium sulphate, the latter is introduced in the amount of 0.1-2% in relation to the weight of nitrate to the ammonium nitrate solution before or after its evaporation, and then mixed with ground lime. 948, ESW "Press", Kielce, The addition of calcium or ammonium sulphate to the calcium ammonium nitrate alloy increases its freezing point compared to the calcium ammonium nitrate alloy without these additives. This phenomenon plays an important role in the granulation process, causing the granule to completely solidify before reaching the bottom A granule of calcium ammonium nitrate without the addition of the above-mentioned salts, reaching the bottom of the tower, is plastic and sticks with others, forming large agglomerates, and moreover, during further processing of nitro-chalk, i.e. cooling, breaking and sorting, it gives a lot of undersize, which floods the sieves, creates Difficulties in the processing of the dust and the deterioration of the properties of the product during its storage By following the method according to the invention, these disadvantages are eliminated, and the product is obtained with a relatively low hygroscopic due to the reduced content of calcium nitrate, and little susceptible to caking. EN

Claims (1)

1. Zastrzezenie patentowe Sposób zmniejszania rozkladu azotanu amono¬ wego zawartego w saletrzaku, znamienny tym, ze podczas wytwarzania saletrzaku, dodaje sie do niego gipsu lub siarczanu amonowego, przy czym gips wprowadza sie do kamienia wapien¬ nego przed jego rozdrobnieniem, stosujac 0,1—3,0% gipsu w stosunku do masy kamienia i nastepnie po zmieleniu miesza ze stezonym roztworem azotanu amonowego, natomiast siar¬ czan amonowy w ilosci 0,1%—2% w stosunku do masy saletrzaku, wprowadza sie do roztworu azotanu amonowego przed lub po jego odpa¬ rowaniu i miesza ze zmielonym kamieniem wapiennym. Zaklady Azotowe „Kedzierzyn" PL1. Patent claim A method of reducing the decomposition of ammonium nitrate contained in calcium ammonium nitrate, characterized in that during the production of nitro-chalk, gypsum or ammonium sulphate is added to it, and the gypsum is introduced into the limestone before its grinding, using 0.1 -3.0% of gypsum in relation to the mass of stone and then, after grinding, mixed with a concentrated solution of ammonium nitrate, while ammonium sulphate in the amount of 0.1% -2% in relation to the mass of calcium ammonium nitrate, is introduced into the ammonium nitrate solution before or after it has been evaporated and mixed with ground limestone. Zakłady Azotowe "Kedzierzyn" PL
PL45932A 1962-03-12 PL45932B1 (en)

Publications (1)

Publication Number Publication Date
PL45932B1 true PL45932B1 (en) 1962-06-15

Family

ID=

Similar Documents

Publication Publication Date Title
AU2007251520C1 (en) Fertilizer granules and manufacturing process thereof
CA2941183C (en) Method for incorporating micronutrients in the outer shell of urea-based particles
US9284232B2 (en) Safe blends of ammonium nitrate (AN) with urea, or of an AN-comprising product with a urea-comprising product
US20100047149A1 (en) Methods for preparing compositions comprising ammonium nitrate double salts
JPS6033795B2 (en) Non-consolidating granular inorganic fertilizer and its manufacturing method
DK165875B (en) PROCEDURE FOR THE MANUFACTURE OF AMMONIUM NITRATE AND CALCIUM CARBONATE CONTAINING FERTILIZERS
PL45932B1 (en)
CZ292236B6 (en) Process for producing calcium nitrate based fertilizers and fertilizer produced in such a manner
US2965444A (en) Noncaking rock salt composition
DE945328C (en) Method and device for the digestion of rock phosphates with nitric acid, in particular for the production of fertilizers
US4594090A (en) High nutrient content fertilizers
EP1093449B1 (en) Ammonium nitrate bodies and a process for their production
SU1724654A1 (en) Process for producing granulated fertilizer
Gissel-Nielsen et al. Ammonia-based flue gas desulphurization waste solution as a nitrogen fertilizer
SU1498744A1 (en) Method of producing complex slowly-soluble fertilizers
US20060010948A1 (en) Nitrogen-potash fertiliser and the method for producing thereof
RU2306304C1 (en) Nitrogen, calcium, and sulfur-containing complex fertilizer manufacturing process
Kolyshkin et al. Production of complex nitrogen-potassium and nitrogen-magnesium fertilizers from substandard urea fractions
RASULOV et al. LIME-AMMONIUM NITRATE BASED ON AMMONIUM NITRATE FUEL AND CHALK.
EA049845B1 (en) METHOD OF PRODUCING GRANULAR ENRICHED AMELIORANT FROM WASTE OF PHOSPHORUS PRODUCTION - PHOSPHOGYPSUM
DE1592585C3 (en)
Gezerman et al. Effects of Fertilizer Compositions Containing Calcium Lignosulfonate and Silicic Acid as an Alternative to Organic Fertilizers to Prevent Caking and Degradation
PL189493B1 (en) Method of obtaining mixed fertilisers containing ammonia nitrogen
PL210140B1 (en) Method of production of organic and mineral fertilizer and the fertilizer
PL134740B1 (en) Method of obtaining granulated ammonium nitrate