CS208902B1 - Reclaiming fertilizer for acid soils based on carbonation scums - Google Patents
Reclaiming fertilizer for acid soils based on carbonation scums Download PDFInfo
- Publication number
- CS208902B1 CS208902B1 CS792987A CS298779A CS208902B1 CS 208902 B1 CS208902 B1 CS 208902B1 CS 792987 A CS792987 A CS 792987A CS 298779 A CS298779 A CS 298779A CS 208902 B1 CS208902 B1 CS 208902B1
- Authority
- CS
- Czechoslovakia
- Prior art keywords
- fertilizer
- sludge
- weight
- sugar
- substrate
- Prior art date
Links
- 239000003337 fertilizer Substances 0.000 claims description 35
- 239000010802 sludge Substances 0.000 claims description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000011707 mineral Substances 0.000 claims description 14
- 235000010755 mineral Nutrition 0.000 claims description 14
- 239000000758 substrate Substances 0.000 claims description 14
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 10
- 230000018044 dehydration Effects 0.000 claims description 8
- 238000006297 dehydration reaction Methods 0.000 claims description 8
- 238000009738 saturating Methods 0.000 claims description 8
- 239000002594 sorbent Substances 0.000 claims description 8
- 239000010451 perlite Substances 0.000 claims description 7
- 235000019362 perlite Nutrition 0.000 claims description 7
- 238000011282 treatment Methods 0.000 claims description 7
- 230000002378 acidificating effect Effects 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 235000015097 nutrients Nutrition 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 230000008569 process Effects 0.000 claims description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 2
- 230000008901 benefit Effects 0.000 claims description 2
- 229940043430 calcium compound Drugs 0.000 claims description 2
- 150000001674 calcium compounds Chemical class 0.000 claims description 2
- 230000008859 change Effects 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 238000010924 continuous production Methods 0.000 claims description 2
- 230000035622 drinking Effects 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 239000011591 potassium Substances 0.000 claims description 2
- 229910052700 potassium Inorganic materials 0.000 claims description 2
- 239000010865 sewage Substances 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 claims 2
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 claims 1
- 101100394220 Clostridium botulinum D phage ha-70 gene Proteins 0.000 claims 1
- 240000000731 Fagus sylvatica Species 0.000 claims 1
- 235000010099 Fagus sylvatica Nutrition 0.000 claims 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims 1
- 235000021536 Sugar beet Nutrition 0.000 claims 1
- 230000002730 additional effect Effects 0.000 claims 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims 1
- 239000001166 ammonium sulphate Substances 0.000 claims 1
- 235000011130 ammonium sulphate Nutrition 0.000 claims 1
- 238000004458 analytical method Methods 0.000 claims 1
- 238000003556 assay Methods 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 239000000969 carrier Substances 0.000 claims 1
- 238000011109 contamination Methods 0.000 claims 1
- 238000009472 formulation Methods 0.000 claims 1
- 239000011521 glass Substances 0.000 claims 1
- 230000008676 import Effects 0.000 claims 1
- 229910052744 lithium Inorganic materials 0.000 claims 1
- 230000004048 modification Effects 0.000 claims 1
- 238000012986 modification Methods 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 235000021049 nutrient content Nutrition 0.000 claims 1
- 239000005416 organic matter Substances 0.000 claims 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 claims 1
- 239000011435 rock Substances 0.000 claims 1
- 239000004576 sand Substances 0.000 claims 1
- 238000009331 sowing Methods 0.000 claims 1
- 238000003860 storage Methods 0.000 claims 1
- 235000012094 sugar confectionery Nutrition 0.000 claims 1
- 239000002699 waste material Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241001310793 Podium Species 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000004720 fertilization Effects 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000006052 feed supplement Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 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
(54) Melioračné hnojivo pre kyslé pódy na báze cukrovarských saturačných kalov(54) Ammonia fertilizer based on sugar saturating sludge
Vynález sa týká melioračného hnojivá pre kyslé pódy na báze cukrovarských saturačných kalov.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to acid fertilizer ameliorative fertilizers based on sugar saturating sludge.
Cukrovarské saturačné kaly vznikajú pri výrobě cukru ako odpadový produkt výrobného procesu. Chemický obsah ich zložiek a priaznivá reakcia pH sú velmi vhodné na meliorovanie kyslých pód. Ich využíváme na tieto účely je velmi stažené a doterajšie spósoby manipulácie a prirodzenej dehydratácie nevyhovuj ú dnešným parametrom manipulácie, přepravy a aplikácie. Súčasná technológia v cukrovare nie je založená na tom, aby cukrovarské saturačné kaly boli svojou štruktúrou a konzistenciou uspósobené požiadavkám 1’ahkej manipulovaternosti, a preto sa hromadia na skládkách pri cukrovaroch, kde vyplavováním l’ahko rozpustného Ca spósobu jú zvyšovanie stupňov tvrdosti podzemných a tečúcich vod. Najpoužívanejším spósobom v cykle saturačné kaly — cukrovar — póda je odstraňovanie saturačných kalov z cukrových štiav vakuovými filtrami, ktoré znižujú obsah vody v saturačných kaloch na 40—60 %. Pri tomto obsahu vody sú saturačné kaly mazlavé, lepivé a súdržné. Před dopravou na skládky sa zvodňujú až po obsah vody 80 % a potom sa hydraulicky dopravujú na skládky. Na skládkách sa podrobujú prirodzenej dehydratácii až po zníženie obsahu vody na 45—55 %, kedy sú ako tak manipulovatelné, ale stále mazlavé. Tento proces „vyzrievania na skládkách“ trvá dva roky. Preberajúce poínohospodárske závody ich deponujú na pódu, na okraj honov, kde majú byť použité a tu ostávajú najmenej 1 rok až po zníženie obsahu vody pod hranicu 30 %, kedy ich možno rozmetat’ rozmetadlami maštalného hnoja. Pretože v celosvetovom meradle ide o velké množstvá a hodnoty, je problém využitia a spracovávania saturačných kalov predmetom velmi frekventovaným. Vo svete sa střetáváme s trojakým použitím saturačných kalov. Regenerujú sa na CaO vypalováním vo viacstupňových peciach, aby mohli byť znova použité k saturovaniu štiav; spracúvajú sa na krmné doplňky pre výživu zvierat. Najširšie použitie je pre hnojenie. Pre potřeby tohto použitia sa v zahraničí používajú k úpravě saturačných kalov s nižším obsahom vody výkonné jšie filtry, sušenie používáním tradičných zdrojov tepelnej energie a pod. Okrem spósobu prirodzenej dehydratácie používanej aj u nás a ktorú sme popísali vyššie, móžeme všetky ostatně úpravy podía ich podstaty zaradiť do týchto spósobov: riedenie vodou a hnojenie rozstrekovaním po pode rieši holandský patent č. 76 754; miešanie so škvárou a popolom získanými spárováním odpadkov a miešaním s dalšími odpadmi s obsahom drasla a pod. rieši rakúsky patent č. 314 567; miešanie s CaO, granuláciu a sušenie švédsky patent č. 355 796. NevýhodouSugar saturation sludge is produced in the production of sugar as a waste product of the production process. The chemical content of their components and the favorable pH reaction are very suitable for ameliorating the acidic pod. Their use for these purposes is very narrow and the current methods of handling and natural dehydration do not meet today's parameters of handling, transport and application. Current technology in the sugar refinery is not based on the saturation sludge of its structure and consistency adapted to the requirements of ease of handling, and therefore accumulates in landfill sites at sugar refineries where leaching of readily soluble Ca causes increasing hardness levels of underground and flowing water. The most used method in the saturation sludge - sugar refinery - podium cycle is to remove the saturation sludge from the sugar juices by vacuum filters, which reduce the water content of the saturation sludge to 40-60%. At this water content, the saturation sludge is sticky, sticky and cohesive. Before being transported to landfills, they are watered up to a water content of 80% and then hydraulically transported to landfills. In landfills they undergo natural dehydration only after the water content has been reduced to 45-55%, when they are still manageable, but still sticky. This process of 'landfill maturation' takes two years. Receiving farms deposit them on the podium, on the edge of the farms where they are to be used and remain there for at least 1 year, up to a reduction of the water content below 30%, where they can be spread by manure spreaders. Because these are large quantities and values worldwide, the problem of utilization and processing of saturation sludge is a very frequent subject. In the world we encounter the triple use of saturation sludge. They are regenerated to CaO by firing in multi-stage furnaces so that they can be reused to saturate the juices; they are processed into animal feed supplements. The widest application is for fertilization. For the purpose of this application, more efficient filters, drying using traditional sources of thermal energy, etc. are used abroad to treat saturating sludges with lower water content. In addition to the method of natural dehydration also used in the Czech Republic and described above, all other treatments according to their nature can be included in the following ways: dilution with water and spray fertilization on the floor are covered by Dutch patent no. 76 754; mixing with clinker and ash obtained by grouting waste and mixing with other potassium containing wastes and the like. is the subject of Austrian patent no. 314 567; mixing with CaO, granulating and drying Swedish patent no. 355 796. The disadvantage
208 902 předmětných riešení je náročnost’ na dovoz výkonných filtrov zo zahraničia, spotřeba nedostatkových ušlachtilých zdrojov energie alebo obmedzené miestne použitie. V případe využívania prirodzenej dehydratácie je nevýhodou súdržná mazlavá konzistencia, zlá manipulovatelnosť, dlhá doba skladovania a nebezpečie kontaminácie pitných a úžitkových vód vápenatými zlúčeninami v okolí skládok.208 902 of the solutions in question are the difficulty of importing high-performance filters from abroad, the consumption of scarce noble energy sources or limited local use. In the case of the use of natural dehydration, the disadvantage is a cohesive sticky consistency, poor handling, long shelf life and the risk of calcium compounds contaminating drinking and process water around landfills.
Vyššie uvedené nedostatky odstraňuje melioračné hnojivo pre kyslé pódy na báze cukrovarských saturačných kalov, tvořené z 65—90 % hmotnostných % cukrovarských saturačných kalov s obsahom vody od 40 do 60 % a od 5 do 16 hmotnostných % minerálneho sorbentu. Táto zmes móže byť ďalej spracovávaná účinkami 10 hmotnostných· % CaO a doplněná minerálnymi živinami podTa bilančnej potřeby pódy a plodiny, pre ktoré je melioračné hnojivo určené. Po dehydratácii saturačných kalov je možné zo substrátu ešte před jeho zmiešaním s CaO odseparovať časť použitého minerálneho sorbentu cyklónovým odlučovačom a to v prípadoch, kedy má byť melioračný hnojivový substrát respektive hnojivo použité pre Tahké a piesčité pódy. V ťažkých a stredne ťažkých pódach je minerálny sorbent — expandovaný perlit v hnojivé žiadúci pre svoj specifický zúrodňujúci účinok pre tieto druhy pód.The aforementioned drawbacks are eliminated by an acid fertilizer amelioration fertilizer based on sugar saturation sludge consisting of 65-90% by weight sugar saturation sludge with a water content of 40 to 60% and from 5 to 16% by weight of mineral sorbent. This mixture can be further treated with 10% by weight CaO and supplemented with mineral nutrients according to the balance needs of the soil and crop for which the amelioration fertilizer is intended. After dehydration of the saturating sludge, it is possible to separate some of the mineral sorbent used by the cyclone separator from the substrate prior to its mixing with CaO, in cases where the fertilizer substrate or the fertilizer is to be used for heavy and sandy soil. In difficult and moderate stages, the mineral sorbent - expanded perlite in fertilizer is desirable for its specific fertilising effect for these types of stages.
Přednostou navrhovaného riešenia je zásadná změna mazlavej konzistencie cukrovarských saturačných kalov na hmotu sypkej konzistencie a jemnej zrnitosti, ktorá sa dosahuje už pri vlhkosti substrátu na hranici 40 % vlhkosti. Vyššia stabilita získanej jemnej zmítej štruktúry sa dosiahne pósobením přidaného CaO. Účinnost’ úpravy sa najviac prejavuje v 1’ahkej manipulovatelnosti takto připraveného substrátu, ďalej umožní zaviesť kontinuálny proces úpravy saturačných kalov na^ vázujúci na celkový proces výroby cukru. To umožní využiť dopravné prostriedky použité na dopravu cukrovej řepy k spátnej preprave melioračného hnojivá. V samotnej prevádzke cukrovaru sa podstatné zníži spotřeba vody potrebnej na zvodňovanie kalov pre ich hydraulickú dopravu na skládky. Zníži sa tiež potřeba skládkovej plochy a vylúči sa nebezpečie zvyšovania tvrdosti vód kontaminovanými splaškami a priesakmi zo skládok. Pre pornohospodárstvo sa získá zdroj velmi hodnotných melioračných a hnojivových živin, ktorých sú saturačné kaly nositeíom. Úpravou sa dosahuje rovnoměrná, velmi jemná zrnitost’ substrátu a ich sypká konzistencia umožňuje používat’ k manipulácii, preprave a aplikácii strojový park určený pre sypké hmoty respektive pre přepravu a aplikáciu minerálnych hnojiv.The advantage of the proposed solution is a fundamental change of the sticky consistency of sugar saturating sludge to a mass of loose consistency and fine grain size, which is already achieved at the substrate moisture level of 40% moisture. The higher stability of the obtained fine milling structure is achieved by imparting added CaO. The efficiency of the treatment is most evident in the ease of manipulation of the substrate thus prepared, further allowing the introduction of a continuous process for the treatment of the saturation sludge to the total sugar production process. This will make it possible to use the means of transport used to transport the beet for the return transport of the ameliorative fertilizer. In the operation of the sugar refinery itself, the water consumption necessary for watering the sludge for its hydraulic transport to landfills is substantially reduced. The need for landfill sites will also be reduced and the risk of increasing water hardness by contaminated sewage and leakage from landfills will be eliminated. A source of very valuable amelioration and fertilizer nutrients, the saturation sludge of which is the bearer, is obtained for the porn economy. The treatment achieves a uniform, very fine grain size of the substrate and its loose consistency makes it possible to use, for handling, transport and application, the machinery intended for loose materials and for the transport and application of mineral fertilizers.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS792987A CS208902B1 (en) | 1979-05-02 | 1979-05-02 | Reclaiming fertilizer for acid soils based on carbonation scums |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS792987A CS208902B1 (en) | 1979-05-02 | 1979-05-02 | Reclaiming fertilizer for acid soils based on carbonation scums |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CS208902B1 true CS208902B1 (en) | 1981-10-30 |
Family
ID=5368641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS792987A CS208902B1 (en) | 1979-05-02 | 1979-05-02 | Reclaiming fertilizer for acid soils based on carbonation scums |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS208902B1 (en) |
-
1979
- 1979-05-02 CS CS792987A patent/CS208902B1/en unknown
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