DK169569B1 - Use of a mixture which comprises a nitrogen-containing fertiliser and a strong mineral acid as a slurry- improving agent for decreasing ammonia evaporation therefrom, a slurry product with decreased ammonia evaporation, and a process for producing such a product - Google Patents
Use of a mixture which comprises a nitrogen-containing fertiliser and a strong mineral acid as a slurry- improving agent for decreasing ammonia evaporation therefrom, a slurry product with decreased ammonia evaporation, and a process for producing such a product Download PDFInfo
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- DK169569B1 DK169569B1 DK008293A DK8293A DK169569B1 DK 169569 B1 DK169569 B1 DK 169569B1 DK 008293 A DK008293 A DK 008293A DK 8293 A DK8293 A DK 8293A DK 169569 B1 DK169569 B1 DK 169569B1
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- DK
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- Prior art keywords
- slurry
- mixture
- product
- manure
- ammonia evaporation
- Prior art date
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- 239000002002 slurry Substances 0.000 title claims description 76
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims description 32
- 239000000203 mixture Substances 0.000 title claims description 28
- 239000002253 acid Substances 0.000 title claims description 23
- 229910021529 ammonia Inorganic materials 0.000 title claims description 16
- 239000003337 fertilizer Substances 0.000 title claims description 16
- 238000001704 evaporation Methods 0.000 title claims description 15
- 230000008020 evaporation Effects 0.000 title claims description 15
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims description 11
- 239000011707 mineral Substances 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 8
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 title claims description 3
- 239000003795 chemical substances by application Substances 0.000 title description 24
- 230000003247 decreasing effect Effects 0.000 title 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 51
- 210000003608 fece Anatomy 0.000 claims description 31
- 239000010871 livestock manure Substances 0.000 claims description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000003623 enhancer Substances 0.000 claims description 18
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 13
- 239000004202 carbamide Substances 0.000 claims description 13
- 239000000654 additive Substances 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 9
- 241000283690 Bos taurus Species 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 239000000618 nitrogen fertilizer Substances 0.000 claims description 7
- 238000002360 preparation method Methods 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 150000002739 metals Chemical class 0.000 claims description 5
- 239000000975 dye Substances 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 claims description 2
- 239000011701 zinc Substances 0.000 claims description 2
- 229910052725 zinc Inorganic materials 0.000 claims description 2
- -1 and if desired Substances 0.000 claims 1
- 239000000047 product Substances 0.000 description 22
- 238000003756 stirring Methods 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 8
- 235000010755 mineral Nutrition 0.000 description 8
- 150000007513 acids Chemical class 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 229910017604 nitric acid Inorganic materials 0.000 description 3
- 229910019142 PO4 Inorganic materials 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000004063 acid-resistant material Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- YYRMJZQKEFZXMX-UHFFFAOYSA-L calcium bis(dihydrogenphosphate) Chemical compound [Ca+2].OP(O)([O-])=O.OP(O)([O-])=O YYRMJZQKEFZXMX-UHFFFAOYSA-L 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910000150 monocalcium phosphate Inorganic materials 0.000 description 1
- 235000019691 monocalcium phosphate Nutrition 0.000 description 1
- 210000004400 mucous membrane Anatomy 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Fertilizers (AREA)
Description
i DK 169569 B1in DK 169569 B1
Opfindelsen angår anvendelse af en blanding omfattende en nitrogenholdig kunstgødning og en stærk mineralsk syre som gylleforbedringsmiddel til nedsættelse af ammoniakfordampning herfra, gylleprodukt med nedsat 5 ammoniakfordampning samt fremgangsmåde til fremstilling af et sådant produkt.BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to the use of a mixture comprising a nitrogenous fertilizer and a strong mineral acid as a slurry enhancer for reducing ammonia evaporation thereof, a slurry product with reduced ammonia evaporation, and a process for producing such a product.
Ammoniakfordampning efter udspredning på markoverflader af gylle bærer ansvaret for et stort nitrogentab fra gyllen. Hermed nedsættes gyllens værdi som 10 gødning og den fordampede ammoniak kan, opløst i regnvand, medføre forurening med nitrogen på uønskede steder, eksempelvis af søer og vandløb. Den dårlige udnyttelse af nitrogen i gyllen medfører et større gødningsforbrug i form af gylle. Efter dansk lovgivning kan 15 gylle ikke udbringes hele året, da der på visse tidspunkter er en stor risiko for udvaskning. Dette betyder, at landbruget skal kunne opbevare gyllen i flere måneder, og næsten alle landbrug med animalsk produktion har da også i dag en gylletank. Størrelsen kan va-20 riere meget, men er i gennemsnit omkring 2000 m3.Ammonia evaporation after dispersal on slurry field surfaces is responsible for a large loss of nitrogen from the slurry. This reduces the value of manure as 10 fertilizers and the evaporated ammonia can, dissolved in rainwater, cause pollution with nitrogen in undesirable places, for example by lakes and streams. The poor utilization of nitrogen in the slurry results in a higher fertilizer consumption in the form of slurry. Under Danish law, 15 slurries cannot be released all year, as there is a high risk of leaching at certain times. This means that agriculture must be able to store manure for months, and almost all farms with animal production have a manure tank today. The size can vary greatly, but is on average about 2000 m3.
Når udbringningen af gylle skal finde sted, normalt i perioderne marts/juni og i efterårsmånederne september/november, kontakter landmanden ofte sin maskinstation, der sørger for udbringningen. Denne proces 25 er dyr, da de maskiner der bruges er meget dyre. Når gyllen er udbragt, vil landmanden typisk på et senere tidspunkt i foråret gødske med en anden gødning for at få optimalt udbytte.When the manure is to be dispensed, usually during the months of March / June and in the autumn months of September / November, the farmer often contacts his machine station to arrange the application. This process 25 is expensive as the machines used are very expensive. When the manure is applied, the farmer will typically fertilize at a later stage in the spring with another fertilizer to get optimum yield.
Problemet diskuteres af R.J. Stevens et. al., J.The problem is discussed by R.J. Stevens et. al., J.
30 Agricultural Science, 113 (1989) 389-395, hvor også ældre referencer til emnet angives. Det nævnes, at 24-80% af ammoniumnitrogen kan mistes inden for den første uge efter udbringning af gyllen på markoverflader. Problemet bliver mindre, hvis gyllen nedharves umiddelbart 35 efter udbringningen eller i forbindelse med udbringningen injiceres i markoverfladen. Allerede i 1938 fandt DK 169569 B1 2 man imidlertid, at dette kunne undgås, hvis man sænkede pH i gyllen med henblik på reduktion af ammoniakfordampningen fra denne. Man fandt, at phosphorsyre og mo-nocalciumphosphat var effektive midler til en sådan 5 sænkning af pH i gyllen. Disse tilsætningsstoffer er imidlertid ikke billige og anvendelsen af dem kan derudover medføre en overgødsning med phosphat. Af denne grund er andre mineralske syrer, såsom svovlsyre og salpetersyre blevet foreslået til formålet, da disse 10 kemikalier er billigere end de ovenfor anvendte.30 Agricultural Science, 113 (1989) 389-395, which also mentions older references to the subject. It is mentioned that 24-80% of ammonium nitrogen can be lost within the first week after application of slurry on field surfaces. The problem becomes less if the slurry is degraded immediately after the application or in connection with the application is injected into the field surface. However, as early as 1938, DK 169569 B1 2 found that this could be avoided if the pH of the slurry was lowered in order to reduce the ammonia evaporation from it. Phosphoric acid and monocalcium phosphate were found to be effective agents for such a lowering of pH in the slurry. However, these additives are not cheap and their use can also cause phosphate overgrazing. For this reason, other mineral acids such as sulfuric acid and nitric acid have been proposed for the purpose, as these 10 chemicals are cheaper than the ones used above.
Således kendes fra DE offentliggørelsesskrift nr. 3 826 247 en fremgangsmåde til oparbejdning af især gylle ved tilsætning af så meget stærk mineralsk syre, især svovlsyre eller phosphorsyre, at pH-værdien heri 15 fortrinsvis bliver 5,5-6,5. Det herved opnåede produkt kan efter inddampning og tørring udspredes som gødning.Thus, from DE Publication No. 3,826,247, a process for working up especially manure by adding so much strong mineral acid, especially sulfuric acid or phosphoric acid, is known that the pH value herein is preferably 5.5-6.5. The product thus obtained can be spread as fertilizer after evaporation and drying.
Nedenstående tabel illustrerer sammenhængen mellem det procentiske tab af ammoniaknitrogen (kumulativt efter 3,25 dage) og værdien af pH i gyllen fra 20 henholdsvis svinegylle (3 forsøgsprøver, S2 og S3) og kvæggylle (3 forsøgsprøver, K1# K2 og K3).The following table illustrates the relationship between the percentage loss of ammonia nitrogen (cumulatively after 3.25 days) and the value of the pH of the slurry from 20 porcine manure (3 test samples, S2 and S3) and cattle manure (3 test samples, K1 # K2 and K3).
_TABEL_ _EH_ 25 Gylle_7,0 6,0 5,5 5,0 4,5 4,0_ TABLE_ _EH_ 25 Slurry_7.0 6.0 5.5 5.0 4.5 4.0
Sx 26,5 3,8 1,7 1,5 0,9 0,8 52 23,4 3,5 2,9 2,2 0,4 0,4 53 19,7 5,6 3,7 1,8 1,6 0,8Sx 26.5 3.8 1.7 1.5 0.9 0.8 52 23.4 3.5 2.9 2.2 0.4 0.4 53 19.7 5.6 3.7 1, 8 1.6 0.8
Middel 23,2 4,3 2,8 1,9 0,9 0,7 30 Κχ 28,7 8,1 1,5 1,7 1,0 0,3 K2 22,9 7,0 1,9 0,6 0,6 0,5 K3 34,4 7,1 0,5 0,6 0,4 0,3Mean 23.2 4.3 2.8 1.9 0.9 0.7 30 ,7 28.7 8.1 1.5 1.7 1.0 0.3 K2 22.9 7.0 1.9 0 , 6 0.6 0.5 K3 34.4 7.1 0.5 0.6 0.4 0.3
Middel_28,6 7,4 1,3 1,0 0,6 0,4Mean_28.6 7.4 1.3 1.0 0.6 0.4
Det ses, at nitrogentabet er stort ved pH 7,0, men falder kraftigt, når pH sænkes under denne værdi.It is seen that the nitrogen loss is large at pH 7.0 but decreases sharply when the pH is lowered below this value.
35 3 DK 169569 B135 3 DK 169569 B1
Husted et. al., J. Sci. Food Agric 57 (1991) 335-349, har undersøgt effekten på pH af at sætte syrer eller forskellige salte til gylle og fandt, at syrer havde den bedste virkning i denne forbindelse, idet pH 5 i gylle ganske vist kunne nedbringes ved salttilsætning, men pH-værdien steg igen efter beluftning af gyllen.Husted it. al., J. Sci. Food Agric 57 (1991) 335-349, has investigated the effect on pH of adding acids or various salts to manure and found that acids had the best effect in this regard, although pH 5 in manure could be reduced by salt addition, but The pH increased again after aeration of the slurry.
Det vil ses, at ovenstående problem i og for sig kan løses, hvis man sætter så meget syre (fortrinsvis 10 svovlsyre, men andre stærke mineralske syrer kan også anvendes) til gyllen, at dennes pH nedsættes til en værdi i området 4-5. Imidlertid er det utilrådeligt, at landmanden lokalt arbejder med stærke syrer, da det eksempelvis ikke er uden risiko at skulle arbejde med 15 svovlsyre, hvorfor visse sikkerhedskrav ihvertfald må overholdes i denne forbindelse.It will be seen that the above problem can in itself be solved if you add so much acid (preferably 10 sulfuric acid, but other strong mineral acids can also be used) to the slurry that its pH is reduced to a value in the range 4-5. However, it is not advisable for the farmer to work locally with strong acids, as, for example, it is not without risk of having to work with 15 sulfuric acid, which is why certain safety requirements must at least be complied with in this regard.
Der er således behov for et gylleforbedringsmiddel, der kan nedsætte pH i gylle til en værdi i området 4-5 og som endvidere er billigt og mindre farligt at 20 arbejde med end svovlsyre.There is thus a need for a slurry improver which can lower the pH of slurry to a value in the range 4-5 and which is also cheaper and less dangerous to work with than sulfuric acid.
Fra US patentskrift nr. 4 315 763 kendes et væskeformigt gødningsprodukt med en pH-værdi mellem 1,5-4 og som omfatter reaktionsproduktet mellem urinstof og phosphorsyre og eventuelt også reaktionsproduktet mel-25 lem urinstof og svovlsyre samt eventuelt kaliumchlorid og sporelementer. Det nævnes udtrykkeligt, at man ved fremstillingen af dette produkt ikke skal tilsætte vand udover, hvad der allerede findes i de anvendte syrer, og det hverken nævnes eller antydes, at produktet kan 30 benyttes til at nedsætte pH-værdien i gylle med henblik på at formindske ammoniakfordampning fra gyllen.U.S. Patent No. 4,315,763 discloses a liquid fertilizer product having a pH value between 1.5-4 and comprising the reaction product between urea and phosphoric acid and optionally also the reaction product between urea and sulfuric acid and optionally potassium chloride and trace elements. It is explicitly mentioned that in the manufacture of this product, water should not be added beyond what is already present in the acids used, and it is neither mentioned nor implied that the product can be used to reduce the pH in slurry in order to reduce ammonia evaporation from the slurry.
Tilsvarende reaktionsprodukter eller blandinger kendes også i princippet fra US patentskrifterne nr.Corresponding reaction products or mixtures are also known in principle from US Pat.
4 310 343, 4 397 675 og 4 962 283, men heller ikke her 35 nævnes eller antydes blandingernes anvendelighed til nedsættelse af ammoniakfordampning fra gylle.Nos. 4,310,343, 4,397,675, and 4,962,283, but neither here nor are 35 mentioned the applicability of the mixtures for reducing slurry ammonia vaporization.
DK 169569 B1 4DK 169569 B1 4
Det er nu overraskende blevet fundet, at en blanding af ovennævnte art, som er på væskeform og har en pH-værdi under 2, med held kan benyttes til at nedsætte pH i gylle til de ovenfor nævnte ønskede værdier, 5 og samtidigt er langt mindre farligt at arbejde med end svovlsyre.It has now surprisingly been found that a mixture of the aforementioned kind which is in liquid form and having a pH below 2 can be successfully used to reduce the pH of slurry to the above-mentioned desired values, 5 and at the same time is much less dangerous to work with than sulfuric acid.
Hvis landmanden sætter et sådant middel til gyllen lige før eller under udbringningen af denne, vil fordampningen af gylle blive reduceret, i kvæggylle med 10 op til 95% og i svinegylle op til 82%, hvilket betyder langt bedre udnyttelse af gyllen, langt mindre lugtgener for omgivelserne og mindre nitrogenforurening af vandløb og søer i omegnen, samt at landmanden ved denne ene udbringning af gyllen vil være i stand til at fuld-15 gødske sin mark uden behov for eftergødskning. Dette betyder endvidere en sparet kørsel, typisk på DKK 100 pr. ha.If the farmer puts such a remedy on slurry just before or during its application, the evaporation of slurry will be reduced, in cattle slurry by 10 up to 95% and in pig slurry up to 82%, which means far better utilization of slurry, far less odor nuisance. for the environment and less nitrogen pollution of streams and lakes in the surrounding area, and that by this one application of the manure the farmer will be able to fertilize his field without the need for fertilizer. This also means a saved drive, typically at DKK 100 per day. ha.
I overensstemmelse hermed angår opfindelsen en anvendelse af en blanding på væskeform og med en pH-20 værdi under 2, idet blandingen er fremstillet ud fra en nitrogenholdig kunstgødning valgt blandt N-, NP- og NPK-gødninger eller blandinger deraf, en stærk mineralsk syre og vand, samt om ønsket additiver, som gylleforbedringsmiddel til nedsættelse af ammoniakfordamp-25 ningen fra udbragt gylle.Accordingly, the invention relates to the use of a liquid form mixture having a pH value below 2, the mixture being prepared from a nitrogenous fertilizer selected from N, NP and NPK fertilizers or mixtures thereof, a strong mineral acid and water, as well as, if desired, additives, as slurry enhancers to reduce ammonia evaporation from slurry.
Blandingen, der benyttes ved anvendelsen ifølge opfindelsen vil i det følgende blive benævnt den omhandlede blanding eller det omhandlede gylleforbedringsmiddel .The mixture used in the application of the invention will hereinafter be referred to as the present blend or slurry enhancer.
30 Den nitrogenholdige kunstgødning er fortrinsvis en N-gødning, der i det væsentlige omfatter urinstof, og den stærke mineralske syre er fortrinsvis svovlsyre.The nitrogenous fertilizer is preferably an N fertilizer which essentially comprises urea and the strong mineral acid is preferably sulfuric acid.
Det omhandlede gylleforbedringsmiddel er fortrinsvis fremstillet (pr. 1000 kg blanding) ud fra 35 50-350 kg urinstof og 200-350 kg koncentreret svovlsyre og resten vand, idet vandmængden ligger indenfor områ- 5 DK 169569 B1 det 300-700 kg. De angivne grænser for vægtmængden af koncentreret svovlsyre svarer til en 96 vægt% svovlsyre, og grænserne må ændres tilsvarende, hvis den koncentrerede svovlsyre har en anden styrke.The slurry improvement agent is preferably prepared (per 1000 kg of mixture) from 50 to 350 kg of urea and 200 to 350 kg of concentrated sulfuric acid and the remainder of water, the amount of water being within the range of 300-700 kg. The limits stated for the weight amount of concentrated sulfuric acid correspond to a 96% by weight sulfuric acid and the limits must be changed accordingly if the concentrated sulfuric acid has a different strength.
5 Den omhandlede blanding kan yderligere omfatte op til 2 vægt%, baseret på totalvægten af tilsat vand, mineralsk syre og nitrogenholdig kunstgødning, af additiver omfattende. spormetaller udvalgt blandt zink, mangan, aluminium, magnesium, kobber og jern, og/eller 10 farvestoffer.The composition of the present invention may further comprise up to 2% by weight, based on the total weight of added water, mineral acid and nitrogenous fertilizers, of additives comprising. trace metals selected from zinc, manganese, aluminum, magnesium, copper and iron, and / or 10 dyes.
Spormetallerne kan tilsættes på form af billige uorganiske forbindelser, der er vandopløselige eller i hvertfald syreopløselige.The trace metals can be added in the form of cheap inorganic compounds which are water soluble or at least acid soluble.
Anvendelsen ifølge opfindelsen er i en foretruk-15 ket udførelsesform en sådan, hvorved a) indholdet i gylletanken omrøres grundigt og blandingen som ovenfor defineret tilsættes, hvorefter den således forbedrede gylle samme dag eller senest næste dag udbringes, eller 20 b) blandingen som ovenfor defineret fyldes i gyllevognen, hvorefter der fyldes op med gylle og den således forbedrede gylle udbringes, eller c) blandingen som ovenfor defineret under udbringning af gylle sættes til gyllen i gyllevognens fordeler-25 system, idet der i alle tilfælde benyttes 1-5 kg, og fortrinsvis 3-4 kg af blandingen som ovenfor defineret pr. 100 kg gylle.The use according to the invention is, in a preferred embodiment, one in which: a) the contents of the slurry tank are thoroughly stirred and the mixture as defined above is added, after which the improved slurry is thus dispensed on the same day or latest the next day, or b) the mixture as defined above. (c) the mixture as defined above during application of slurry is added to the slurry in the slurry distributor system, using in each case 1-5 kg, and preferably 3-4 kg of the mixture as defined above. 100 kg slurry.
Det omhandlede gylleforbedringsmiddel er en klar 30 væske med en pH-værdi i området fra lidt over 0 og til under 2, fortrinsvis op til 1,5. Af sikkerhedsgrunde kan produktet farves, og fagmanden kender farvestoffer, der er stabile i svovlsur opløsning. Forsøg har vist, at det omhandlede gylleforbedringsmiddel er uskadeligt 35 for mennesker, idet det ikke ved kortvarig kontakt på huden virker ætsende på denne. Hvis produktet kommer i DK 169569 B1 6 kontakt med slimhinder, såsom i kontakt med øjet, vil der optræde en sviende fornemmelse, og man bør straks skylle med koldt vand. Midlet er imidlertid ætsende overfor metaller, og skal derfor opbevares i specielle 5 plasttanke eller coatede metaltanke.The present slurry enhancer is a clear liquid having a pH in the range of just over 0 to below 2, preferably up to 1.5. For safety reasons, the product can be dyed and those skilled in the art will know dyes which are stable in sulfuric acid solution. Studies have shown that the manure enhancer in question is harmless to humans, as it does not corrosive to it on short contact with the skin. If the product comes into contact with mucous membranes, such as in contact with the eye, a sensation of burning will occur and you should immediately rinse with cold water. However, the agent is corrosive to metals and must therefore be stored in special plastic tanks or coated metal tanks.
Hvis der i forbindelse med lagring eller anvendelse af den omhandlede blanding optræder en udsivning, kan produktet blot neutraliseres med kalk, eller den med produktet forurenede jord kan opgraves og spredes 10 ud over en mark, hvorved marken samtidig bliver gødet.If, during storage or use of the composition in question, a leakage occurs, the product can simply be neutralized with lime, or the soil contaminated with the product can be excavated and spread over a field, thereby simultaneously fertilizing the field.
Det omhandlede gylleforbedringsmiddel kan fremstilles ved en fremgangsmåde, hvorved man i en syrefast beholder forsynet med en kraftig omrører i rækkefølge og under omrøring indfører vand, de eventuelle additi-15 ver, den nitrogenholdige kunstgødning, og den stærke mineralske syre til dannelse af det omhandlede gylleforbedringsmiddel på væskeform, hvorefter man aftapper produktet.The manure enhancer of the invention may be prepared by a process whereby in an acid-resistant container provided with a powerful stirrer in order and with stirring, water, any additives, the nitrogenous fertilizer and the strong mineral acid to form the manure enhancer, are introduced. in liquid form, after which the product is drained.
Denne fremgangsmåde udføres fortrinsvis ved, at 20 man i en syrefast beholder forsynet med en kraftig omrører pr. 1000 kg blanding, beregnet uden eventuelle additiver, under omrøring indfører: 300-700 kg vand, eventuelle additiver i mængder som angivet 25 ovenfor, og 50-350 kg urinstof, hvorefter man under fortsat omrøring til den stærkt afkølede blanding fører 200-350 kg koncentreret svovlsyre, beregnet som 96 vægt% svovlsyre, 30 til dannelse af det omhandlede gylleforbedringsmiddel på væskeform, hvorefter man aftapper produktet.This method is preferably carried out by providing a strong stirrer in an acid-resistant container per minute. 1000 kg of mixture, calculated without any additives, with stirring introduces: 300-700 kg of water, any additives in quantities as indicated above, and 50-350 kg of urea, then with continued stirring to the strongly cooled mixture 200-350 kg concentrated sulfuric acid, calculated as 96% by weight of sulfuric acid, to give the liquid slurry enhancer in question and the product is then drained off.
Det omhandlede gylleprodukt med nedsat ammoniakfordampning er ejendommeligt ved, at det omfatter sædvanlig gylle, især svinegylle eller kvæggylle, hvortil 35 pr. 100 kg gylle er sat 1-5 kg, og fortrinsvis 3-4 kg af gylleforbedringsmidlet som ovenfor defineret.The manure product with reduced ammonia evaporation is peculiar in that it comprises conventional manure, especially pig manure or cattle manure, to which 35 100 kg slurry is set at 1-5 kg and preferably 3-4 kg of slurry enhancer as defined above.
7 DK 169569 B17 DK 169569 B1
Gylleproduktet kan ifølge opfindelsen fremstilles ved en fremgangsmåde der er ejendommelig ved, at man til sædvanlig gylle, såsom svinegylle eller kvæggylle pr. 100 kg gylle sætter 1-5 kg, og fortrinsvis 5 3-4 kg, af det væskeformige gylleforbedringsmiddel som ovenfor defineret.The manure product according to the invention can be prepared by a method which is characterized in that by conventional manure, such as pig manure or cattle manure per day. 100 kg slurry puts 1-5 kg, and preferably 5 3-4 kg, of the liquid slurry enhancer as defined above.
Opfindelsen vil i det følgende blive nærmere beskrevet under henvisning til fremstillingseksempler (1-3) og anvendelseseksempler (A-D).The invention will be described in greater detail below with reference to Preparation Examples (1-3) and Application Examples (A-D).
10 I en foretrukket udførelsesform af det omhandle de gylleforbedringsmiddel er den ved fremstillingen af midlet anvendte nitrogenholdige kunstgødning en N-gødning, der i det væsentlige omfatter urinstof. Hvis tilførsel af phosphat til markerne i forbindelse med 15 udbringning af gylle ikke er et problem, kan en NP-gødning også anvendes. Forbedringsmidlet er endvidere forsøgt fremstillet under anvendelse af NPK-gødning, men kan i dette tilfælde til en vis grad indeholde udfældede uklarheder og bør omrøres eller omrystes inden 20 brugen.In a preferred embodiment of the manure improvement agent, the nitrogenous fertilizer used in the preparation of the agent is an N-fertilizer which essentially comprises urea. If the application of phosphate to the fields in connection with the application of manure is not a problem, an NP fertilizer can also be used. Furthermore, the enhancer has been attempted using NPK fertilizer, but may in some cases contain precipitated haze and should be stirred or shaken before use.
De stærke mineralske syrer, der indgår i det omhandlede gylleforbedringsmiddel, kan eksempelvis være svovlsyre, saltsyre, salpetersyre, phosphorsyre eller blandinger heraf, fortrinsvis svovlsyre, saltsyre eller 25 salpetersyre og især svovlsyre.The strong mineral acids which are included in the slurry improvement agent can be, for example, sulfuric acid, hydrochloric acid, nitric acid, phosphoric acid or mixtures thereof, preferably sulfuric acid, hydrochloric acid or nitric acid and especially sulfuric acid.
I forbindelse med fremstillingen af midlet benyttes svovlsyren fortrinsvis som koncentreret svovlsyre, såsom en 96 vægt% svovlsyre.In the preparation of the agent, the sulfuric acid is preferably used as concentrated sulfuric acid, such as a 96% by weight sulfuric acid.
Da den ved fremstilling af midlet anvendte syre 30 og selve det omhandlede gylleforbedringsmiddel virker ætsende på metaller, skal der benyttes syrefaste materialer under fremstillingen af midlet til det udstyr, der kommer i kontakt med syren eller med midlet.Since the acid 30 used in the preparation of the agent and the slurry enhancer itself in question acts corrosively to metals, acid-resistant materials must be used during the preparation of the agent for the equipment which comes into contact with the acid or with the agent.
Til en produktion på ca. 10 tons omhandlet gyl-35 leforbedringsmiddel vil man typisk benytte en beholder med et rumfang på ca. 10 m3, eksempelvis fremstillet af 8 DK 169569 B1 PVC eller af epoxycoated jern. Beholderen må være forsynet med en kraftig omrører, såsom en snegl, og omrøringen kan yderligere forbedres ved hjælp af en ledning til recirkulation af indholdet af beholderen fra bund 5 til top af beholderen.For a production of approx. Typically, 10 tonnes of slurry enhancement agent, a container with a volume of approx. 10 m3, for example made of 8 DK 169569 B1 PVC or of epoxy coated iron. The container must be provided with a powerful stirrer, such as a auger, and the stirring can be further enhanced by a conduit for recycling the contents of the container from bottom 5 to the top of the container.
En aftapningsindretning for det fremstillede middel kan med fordel anbringes på den nederste del af denne recirkulationsledning.Advantageously, a tapping device for the manufactured agent may be placed on the lower portion of this recirculation line.
Ved en produktion som ovenfor nævnt anbringer 10 man først den nødvendige vandmængde i beholderen og sætter hertil de nødvendige additiver under omrøring til opløsning eller opslæmning af disse. Herefter tilsættes den anvendte mængde urinstof under kraftig omrøring med sneglen. Det er kendt, at opløsning af urin-15 stof i vand foregår under kraftigt varmeoptag, og man vil da også iagttage, at temperaturen af indholdet i beholderen falder til ned mod 0°C. Når den tilsatte mængde urinstof er opløst, sætter man efter ca. 1 minuts omrøring forsigtigt den nødvendige mængde koncen-20 trerede svovlsyre til indholdet af beholderen og fortsætter omrøringen i ca. 1 minut, hvorefter midlet, der nu på grund af svovlsyrens opløsningsvarme har nået 0 en temperatur i omegnen af 50 C, kan aftappes på en egnet tank eller beholder. Sådanne tanke eller beholdere 25 kan være fremstillet af rustfrit stål eller plast.In a production as mentioned above, 10 first places the required amount of water in the container and adds the necessary additives with stirring to dissolve or slurry them. Then the amount of urea used is added with vigorous stirring with the auger. It is known that dissolution of urine substance in water takes place under heavy heat absorption, and it is then also observed that the temperature of the contents of the container drops to 0 ° C. When the added amount of urea has dissolved, after approx. For 1 minute, gently stir the required amount of concentrated sulfuric acid to the contents of the container and continue stirring for approx. 1 minute, after which the agent, which has now reached 0 a temperature in the region of 50 ° C due to the solution heat of the sulfuric acid, can be drained onto a suitable tank or container. Such tanks or containers 25 may be made of stainless steel or plastic.
Forbedringsmiddel er som nævnt en vandklar væske med en pH-værdi under 2 og har en vægtfylde på omkring 1,2 g/cm3. Midlets farve afhænger af de tilsatte farvestoffer.As mentioned, the enhancer is a water-clear liquid with a pH below 2 and has a density of about 1.2 g / cm 3. The color of the agent depends on the added dyes.
30 Når det omhandlede gylleforbedringsmiddel skal blandes med gylle til opnåelse af en gylle med lav ammoniakfordampning, og denne gylle derefter skal udbringes, bør man gå frem som ovenfor nævnt i forbindelse med den foretrukne omhandlede anvendelse. Det omhandle-35 de gylleprodukt bør udbringes med en slæbeslangevogn.When the slurry enhancer in question is to be mixed with slurry to obtain a slurry with low ammonia vaporization and this slurry must then be applied, one should proceed as mentioned above in connection with the preferred use. The manure product in question should be provided with a tow hose trolley.
9 DK 169569 B1 EKSEMPEL· 1 I en PVC-beholder med omrørersnegl og cirkulationsledning, tilførsels- og aftapningsindretninger 5 fremstillede man som ovenfor nærmere beskrevet et omhandlet gylleforbedringsmiddel ud fra 553 kg vand, 217 kg urinstof og 230 kg 96 vægt% svovlsyre pr. 1000 kg produkt. Produktet var vandklart og havde en pH-værdi på 0,95. Vægtfylden var 1,20 g/cm3.EXAMPLE 1 In a PVC container with stirrer auger and circulation line, supply and drainage devices 5, as described above, a slurry improvement agent was prepared from 553 kg water, 217 kg urea and 230 kg 96% by weight sulfuric acid. 1000 kg of product. The product was water clear and had a pH of 0.95. The density was 1.20 g / cm 3.
10 EKSEMPEL· 2EXAMPLE · 2
Man gik frem som i eksempel 1, idet man til fremstillingen af 1000 kg middel benyttede 662 kg vand, 15 108 kg urinstof og 230 kg 96% svovlsyre. Produktet var vandklart med en pH-værdi på 0,95. Vægtfylden var 1,16 g/cm3.Proceed as in Example 1, using 662 kg of water for the preparation of 1000 kg of agent, 15 108 kg of urea and 230 kg of 96% sulfuric acid. The product was water clear with a pH of 0.95. The density was 1.16 g / cm 3.
EKSEMPEL· 3 20EXAMPLE · 3 20
Idet man gik frem som i eksempel 1, fremstillede man et middel ud fra 444 kg vand, 326 kg urinstof og 230 kg 96% svovlsyre pr. 1000 kg produkt. Produktet var vandklart med en pH-værdi på 1,30, vægtfylden var 1,23 25 g/cm3.Proceeding as in Example 1, an agent was prepared from 444 kg of water, 326 kg of urea and 230 kg of 96% sulfuric acid per liter. 1000 kg of product. The product was water clear with a pH of 1.30, the density was 1.23 25 g / cm 3.
EKSEMPEL AEXAMPLE A
Til en svinegylle med en pH 8,0 satte man 3,8 30 vægt% af midlet fra eksempel 1. Det således fremstillede gylleprodukt havde efter omrøring en pH-værdi på 4,73, og værdien var stabil ved nogle dages henstand.To a pig slurry having a pH 8.0, 3.8% by weight of the agent of Example 1. 3.8 was added. The slurry product thus produced had a pH of 4.73 after stirring and the value was stable at some days standing.
35 DK 169569 B1 1035 DK 169569 B1 10
EKSEMPEL BEXAMPLE B
Til en kvæggylle med pH 7,5 satte man 4 vægt% af midlet fra eksempel 1. Gylleproduktet havde efter omrø-5 ring en pH-værdi på 5,1 og værdien var stabil ved nogle dages henstand.To a cattle slurry with pH 7.5, 4% by weight of the agent of Example 1 was added. After stirring, the slurry product had a pH of 5.1 and the value was stable for a few days.
EKSEMPEL CEXAMPLE C
10 Til en svinegylle med pH 8,0 satte man varieren de vægtmængder af midlet fra eksempel 2. Resultatet ses i nedenstående tabel 2.To a pig manure with pH 8.0, the variant was added to the weight amounts of the agent of Example 2. The results are shown in Table 2 below.
_Tabel 2_ 15 Tilsat mængde middel fra eksempel 2Table 2_ 15 Amount of agent added from Example 2
væqt%_pH% wt _pH
1,8 6,89 20 2,7 6,50 3 5,60 3,7 4,80 4 _4,75 25 Det ses, at man i denne gylle kan nedsætte pH til en værdi, der i høj grad nedsætter ammoniakfordampning fra gyllen ved at benytte 3-4 vægt% af et omhandlet forbedringsmiddel, nemlig midlet fra eksempel 2.1.8 6.89 20 2.7 6.50 3 5.60 3.7 4.80 4 _ 4.75 25 It is seen that in this slurry the pH can be reduced to a value which greatly reduces ammonia evaporation from the slurry using 3-4% by weight of a subject enhancer, namely the agent of Example 2.
30 EKSEMPEL DEXAMPLE D
Til en svinegylle med pH 7,7 satte man 1,8 vægt% af forbedringsmidlet fra eksempel 3. Efter omrøring målte man en pH-værdi på 5,81. Ved denne pH-værdi er 35 ammoniakfordampningen allerede noget nedsat. En sammenligning med resultaterne fra ovenstående eksempel C vi- 11 DK 169569 B1 ser dog, at man i dette tilfælde bør benytte noget mere af midlet fra eksempel 3, sandsynligvis omkring 3 vægt%.To a pig manure with pH 7.7 was added 1.8% by weight of the enhancer of Example 3. After stirring, a pH of 5.81 was measured. At this pH the ammonia evaporation is already somewhat reduced. However, a comparison with the results of the above Example C shows that in this case some more of the agent of Example 3 should be used, probably about 3% by weight.
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK008293A DK169569B1 (en) | 1993-01-25 | 1993-01-25 | Use of a mixture which comprises a nitrogen-containing fertiliser and a strong mineral acid as a slurry- improving agent for decreasing ammonia evaporation therefrom, a slurry product with decreased ammonia evaporation, and a process for producing such a product |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK008293A DK169569B1 (en) | 1993-01-25 | 1993-01-25 | Use of a mixture which comprises a nitrogen-containing fertiliser and a strong mineral acid as a slurry- improving agent for decreasing ammonia evaporation therefrom, a slurry product with decreased ammonia evaporation, and a process for producing such a product |
| DK8293 | 1993-01-25 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| DK8293D0 DK8293D0 (en) | 1993-01-25 |
| DK8293A DK8293A (en) | 1994-07-26 |
| DK169569B1 true DK169569B1 (en) | 1994-12-05 |
Family
ID=8089530
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK008293A DK169569B1 (en) | 1993-01-25 | 1993-01-25 | Use of a mixture which comprises a nitrogen-containing fertiliser and a strong mineral acid as a slurry- improving agent for decreasing ammonia evaporation therefrom, a slurry product with decreased ammonia evaporation, and a process for producing such a product |
Country Status (1)
| Country | Link |
|---|---|
| DK (1) | DK169569B1 (en) |
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1993
- 1993-01-25 DK DK008293A patent/DK169569B1/en not_active IP Right Cessation
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| Publication number | Publication date |
|---|---|
| DK8293D0 (en) | 1993-01-25 |
| DK8293A (en) | 1994-07-26 |
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| B1 | Patent granted (law 1993) | ||
| PBP | Patent lapsed |