SU378382A1 - METHOD OF OBTAINING COMPLEX BIOMINERAL FERTILIZER - Google Patents
METHOD OF OBTAINING COMPLEX BIOMINERAL FERTILIZERInfo
- Publication number
- SU378382A1 SU378382A1 SU1632822A SU1632822A SU378382A1 SU 378382 A1 SU378382 A1 SU 378382A1 SU 1632822 A SU1632822 A SU 1632822A SU 1632822 A SU1632822 A SU 1632822A SU 378382 A1 SU378382 A1 SU 378382A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- fertilizer
- obtaining complex
- biomineral
- autoclave
- biomineral fertilizer
- Prior art date
Links
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
Известно получение биоминерального удобрени из кератинсодержа.щего сырь путем обработки его щелочью с последующей нейтрализацией кислотой.It is known to obtain biomineral fertilizer from keratin-containing raw material by treating it with alkali, followed by neutralization with acid.
Предложенлый опособ отличаетс от известного т&м, что кератимсодержащее сырье (рога, копыта, щетину, волос, щерсть и т. п.) обрабатывают гидроокисью кали под избыточ«ым давлением 2-5 кг/см, а затем нейтрализуют конценфрирова нной фосфорной кислотой . При этом используют 13%-ный раствор гидроокиси .кали из расчета .расхода 1 ч. гидроокиси «али на 3 ч. сырь , а коицентрарованную кислоту дл нейтрализации берут из расчета 12-20% к весу сырь .The proposed procedure differs from the known t & m that keratim-containing raw materials (horns, hooves, bristles, hair, wool, etc.) are treated with potassium hydroxide under excess pressure of 2-5 kg / cm and then neutralized with concentrated phosphoric acid. . In this case, a 13% hydroxide solution is used. It is calculated on the basis of the consumption of 1 part of hydroxide “ali” for 3 parts of raw material, and the co-centric acid is taken from the calculation of 12–20% by weight of the raw material for neutralization.
ПолучйЕное биоминеральное удобрение с высоким содержанием азота в виде амилокислот , а та|Кже фосфо.рно-каливвых солей и микроэлементов оказывает ст;И1мулИрующее действие на рост овощных .и зерновых культур .The resulting biomineral fertilizer with a high content of nitrogen in the form of amilic acids, and that | Khoze phospho. R-potassium salts and microelements exerts the st; Immunizing effect on the growth of vegetable and grain crops.
Приме.р. В эмалированный автоклав помещают 100 кг рого-копытно1го сырь , 39 кг гидроокиси кали и заливают 260 л воды три 20° С. После загруз|КИ автоклав закрывают и подают в него через барбатер острый пар дл создани давлени 4 кг/см. При этом давлени дисульфидные св зи белка раЗрущаютс в течение 3 час. Образую1щиес в процессе реакции газы отвад т из автокла|Ва через 1,5 час (через конденсатор).Example. 100 kg of horn-and-hoofed raw materials, 39 kg of potassium hydroxide are placed in an enamelled autoclave and 260 liters of water are poured over three 20 ° C. After loading the autoclave, the autoclave is closed and steam is fed into it through a barbater to create a pressure of 4 kg / cm. At this pressure, the disulfide bonds of the protein are DECREASED for 3 hours. The gases formed in the course of the reaction are sludge t from the autoclave | Ba after 1.5 hours (via a condenser).
По окончании -процесса ажтоклавировани прекращают подачу пара и уравнивают давление в автоклаве с атмосферным. Затем полученную массу, имеющую рН 11, охлаждают до 50° С путем подачи воды с температурой 20° С в рубашку автоклава, после чего производ т нейтрализацию раствора до рН 7At the end of the bleaching process, the steam supply is stopped and the pressure in the autoclave is equalized with the atmospheric pressure. Then, the resulting mass, having a pH of 11, is cooled to 50 ° C by supplying water with a temperature of 20 ° C to the jacket of the autoclave, after which the solution is neutralized to pH 7
путем подач;и при перемещивании раствора колцентрированной фосфорной кислоты в количестве 12 кг.by giving; and when moving the solution of the concentrated phosphoric acid in the amount of 12 kg.
В результате получают 400 кг биоминералЬНого удобрени с содерл анием вла.ги 70-75%, минеральных солей (преимущественно фосфорно-калиевых) 6-6,2% и азота 2,1-2,5%.As a result, 400 kg of biomineral fertilizer are obtained with a moisture content of 70-75%, mineral salts (mainly phosphorus-potassium) 6-6.2% and nitrogen 2.1-2.5%.
Предмет изобретени Subject invention
2020
1. Способ получени комплексного бИОминерального удобрени из .кератинсодержащего сырь , включающий обработку последнего 25 щелочью и последующую «ейтрализацию, отличающийс тем, что, с целью получени продукта с более высоким содержанием азота в легко усво емом растени ми виде и богатого фосфорно-калийными сол ми, сырье обраба30 тывают гидроокисью /кали под избыточным давлением 2-5 кг1см, а затем нейтрализуют концентрированной фосфорной кислотой. 2. Способ по п. 1, отличающийс тем, что сырье обрабатывают 13%-лым раствором гидрооамси кали из расчета расхода I ч. гидроокиси кал,и на 3 ч. сырь , а колцентрирова.нную фосфорную кислоту дл нейтрализации берут из расчета 12-20% к .весу сырь .1. A method for producing a complex bio-mineral fertilizer from keratin-containing raw materials, including treating the latter with alkali and subsequent "neutralizing", characterized in that, in order to obtain a product with a higher nitrogen content in an easily assimilable plant form and rich in phosphorous-potassium salts , the raw material is treated with hydroxide / potassium under an overpressure of 2-5 kg1 cm, and then neutralized with concentrated phosphoric acid. 2. The method according to claim 1, characterized in that the feedstock is treated with a 13% potassium hydroamide solution at the rate of 1 part of hydrochloric acid, and for 3 parts of raw material, and the concentrated phosphoric acid for neutralization is taken at the rate of 12- 20% to. Weight of raw materials.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1632822A SU378382A1 (en) | 1971-03-16 | 1971-03-16 | METHOD OF OBTAINING COMPLEX BIOMINERAL FERTILIZER |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1632822A SU378382A1 (en) | 1971-03-16 | 1971-03-16 | METHOD OF OBTAINING COMPLEX BIOMINERAL FERTILIZER |
Publications (1)
Publication Number | Publication Date |
---|---|
SU378382A1 true SU378382A1 (en) | 1973-04-18 |
Family
ID=20468635
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1632822A SU378382A1 (en) | 1971-03-16 | 1971-03-16 | METHOD OF OBTAINING COMPLEX BIOMINERAL FERTILIZER |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU378382A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005056497A1 (en) * | 2003-12-12 | 2005-06-23 | Stefan Szoke | Organic nitrogenous fertiliser |
GB2417725A (en) * | 2004-09-07 | 2006-03-08 | John William Carson | Organic fertiliser based on the potassium salt of a phosphated hydrolysed protein |
-
1971
- 1971-03-16 SU SU1632822A patent/SU378382A1/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005056497A1 (en) * | 2003-12-12 | 2005-06-23 | Stefan Szoke | Organic nitrogenous fertiliser |
GB2417725A (en) * | 2004-09-07 | 2006-03-08 | John William Carson | Organic fertiliser based on the potassium salt of a phosphated hydrolysed protein |
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