WO2023035193A1 - Slow-release coated fertilizer and preparation method therefor - Google Patents

Slow-release coated fertilizer and preparation method therefor Download PDF

Info

Publication number
WO2023035193A1
WO2023035193A1 PCT/CN2021/117481 CN2021117481W WO2023035193A1 WO 2023035193 A1 WO2023035193 A1 WO 2023035193A1 CN 2021117481 W CN2021117481 W CN 2021117481W WO 2023035193 A1 WO2023035193 A1 WO 2023035193A1
Authority
WO
WIPO (PCT)
Prior art keywords
slow
fertilizer
polysiloxane
release coated
group
Prior art date
Application number
PCT/CN2021/117481
Other languages
French (fr)
Chinese (zh)
Inventor
王�华
周传健
梁艳
卢海峰
张晨
Original Assignee
山东大学
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
Application filed by 山东大学 filed Critical 山东大学
Publication of WO2023035193A1 publication Critical patent/WO2023035193A1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C9/00Fertilisers containing urea or urea compounds
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity
    • C05G3/40Mixtures of one or more fertilisers with additives not having a specially fertilising activity for affecting fertiliser dosage or release rate; for affecting solubility
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity
    • C05G3/90Mixtures of one or more fertilisers with additives not having a specially fertilising activity for affecting the nitrification of ammonium compounds or urea in the soil
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G5/00Fertilisers characterised by their form
    • C05G5/30Layered or coated, e.g. dust-preventing coatings
    • C05G5/37Layered or coated, e.g. dust-preventing coatings layered or coated with a polymer
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/42Block-or graft-polymers containing polysiloxane sequences
    • C08G77/44Block-or graft-polymers containing polysiloxane sequences containing only polysiloxane sequences
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/20Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
    • Y02P60/21Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures

Definitions

  • the application relates to a slow-release coated fertilizer and a preparation method thereof, belonging to the field of fertilizer preparation.
  • Silicone polymer materials are a special class of polymer materials, and their unique Si-O segments make them exhibit unique advantages in terms of thermal properties, flexibility, film-forming properties, and hydrophobicity.
  • organosilicon polymers can form a dense protective film on the surface of the substrate, which can still prevent corrosion of the substrate under the action of strong acids and alkalis, and have excellent hydrophobicity.
  • organosilicon polymers Can be used as a hydrophobic coating for slow release of fertilizers.
  • the Pt catalyst is often required in the preparation process of organosilicon polymers, and the cost is relatively high, which hinders the application of organosilicon polymers in the agricultural field.
  • the slow-release effect of existing slow-release fertilizers is poor due to the poor performance of the coating material, which causes the problems of waste of resources and indiscriminate application of fertilizers.
  • the application provides a slow-release coated fertilizer and a preparation method thereof.
  • the uniformity of the coating of the slow-release coated fertilizer is high, which is beneficial to the slow-release of the fertilizer, and the slow-release effect is good; the slow-release package
  • the coating material of the outer layer of the film fertilizer has good hydrophobicity, permeability, film-forming property and reusability, so the low amount of coating material used in the slow-release coated fertilizer has a significant advantage and has a positive effect on protecting the environment;
  • the processing cost of release coated fertilizer is low.
  • a slow-release coated fertilizer which includes fertilizer granules and a film coated outside the fertilizer granules, and the film is made of a silicone polymer material;
  • the organosilicon polymer material is prepared by the Diels-Alder reaction of the modified polysiloxane A and the modified polysiloxane B, and the organopolysiloxane A has at least one substituted olefin in one molecule.
  • the organopolysiloxane B has at least one non-aromatic conjugated diene bond group that undergoes a Diels-Alder reaction with the substituted olefin bond group in one molecule.
  • organopolysiloxane makes it exhibit unique advantages in terms of thermal performance, flexibility, film-forming property, hydrophobicity, etc., and organopolysiloxane forms a dense protective film on the surface of the fertilizer.
  • the mass ratio of the organosilicon polymer material to the fertilizer granules is 0.3%-5%.
  • the upper and lower limits of the mass ratio of the organosilicon polymer material to the fertilizer granules are independently selected from 0.5%, 1%, 2%, 3% or 4%. Selected from 0.5%-5%.
  • the mass ratio of the organosilicon polymer material to the fertilizer particles is 0.3%-3%, more preferably 1%-3%. The control of the mass ratio can not only ensure the integrity of the fertilizer coating, but also reduce the usage of coating materials, and at the same time help to control the optimal release rate of the fertilizer.
  • the particle size of the fertilizer particles is 10-40 mesh.
  • the particle size of the fertilizer particles is 20-30 mesh.
  • the mesh size of the fertilizer granules can make the fertilizer fully released in a suitable time. If it is too large, the nutrients cannot be fully released in a limited time, and finally the fertilizer utilization rate will be reduced; if it is too small, the fertilizer will be completely released before it reaches 28 days. Release, not up to the slow-release fertilizer standard.
  • the fertilizer particles are selected from at least one of urea, NPK compound fertilizer, diammonium phosphate, medium element fertilizer, biological fertilizer and organic fertilizer.
  • the substituted olefin bond group in the modified polysiloxane A may be a maleimide group
  • the non-aromatic dien bond group in the organopolysiloxane B The group is a furoyl group
  • the group containing a substituted olefin bond in the modified polysiloxane A can be a maleimide derivative
  • the group in the organopolysiloxane B Diethylenic groups containing non-aromatic hydrocarbons are furoacetyl derivatives.
  • the group containing a substituted olefin bond in the modified polysiloxane A is a maleimide group
  • the group containing a non-aromatic double olefin bond in the organopolysiloxane B is furoacetyl
  • the modified polysiloxane A and the modified polysiloxane B are cross-linked and polymerized to produce at least one reversible substituted cyclohexenyl group to obtain the silicone polymer material, and the structure of the reversible substituted cyclohexenyl group is as follows:
  • Formula I shows:
  • the modified polysiloxane A and the modified polysiloxane B are reversibly cross-linked and polymerized through multiple maleimide groups and furoacetyl groups, so that the obtained silicone polymer material It is a porous material and can be used as a sustained-release coating material.
  • the grafting rate of the maleimide group in the modified polysiloxane A is X
  • the grafting rate of the furoacetyl group in the modified polysiloxane B is Y
  • the ratio of the grafting rate X to the grafting rate Y is 1:1.2-1.5.
  • the ratio of the grafting rate X to the grafting rate Y is 1:1.2-1.5; more preferably, the ratio of the grafting rate X to the grafting rate Y is 1:1.5, so that the grafted horse The imide group and furoacetyl can fully react to improve the utilization rate of grafting raw materials.
  • the grafting rate X is 8%-20%
  • the grafting rate Y is 5%-25%; preferably, the grafting rate X is 10%-20%, and the grafting rate Y is 12% -twenty four%.
  • the values of the grafting ratio X and the grafting ratio Y can ensure the slow-release effect of the prepared organosilicon polymer material, especially the slow-release effect as a fertilizer coating.
  • the calculation of the grafting ratio of X and Y is carried out according to the following method: Accurately weigh about 1.5g of modified polysiloxane in a conical flask with an analytical balance, add about 20mL of tetrahydrofuran and toluene to dissolve, and then add 0.1mol/ L of hydrochloric acid solution, shake well for 5 minutes, add phenolphthalein indicator, measure the excess acid with calibrated sodium hydroxide standard solution, until the solution changes color. In addition, do a blank sample again for the hydrochloric acid solution. Calculate the amino group concentration and the grafting ratio of X and Y according to the following formula:
  • V 0 the volume of sodium hydroxide consumed for titrating the blank sample (mL);
  • V the volume of sodium hydroxide consumed by the titration sample (mL);
  • the polysiloxane A and the polysiloxane B are independently selected from poly(diorganosiloxanes).
  • polysiloxane A has a structural formula as shown in Formula II:
  • R1, R2, R3 and R4 are independently selected from one of hydrocarbon groups, substituted hydrocarbon groups, heteroaryl groups, substituted heteroaryl groups and non-hydrocarbon substituents; m1 and n1 are respectively taken from integers>0, the formula
  • the weight-average molecular weight of the aminated polysiloxane A of II is 2000-20000, and the grafting rate of amino groups in the aminated polysiloxane A is 3%-30%;
  • the R 1 , R 2 , R At least one of 3 and R 4 is linked to the maleimide group of the reversibly substituted cyclohexenyl of formula I.
  • R5, R6, R7 and R8 are independently selected from one of hydrocarbon groups, substituted hydrocarbon groups, heteroaryl groups, substituted heteroaryl groups and non-hydrocarbon substituents; m2 and n2 are respectively taken from integers>0, the formula
  • the weight average molecular weight of the aminated polysiloxane B of III is 2,000 to 20,000, and the grafting rate of amino groups in the aminated polysiloxane B is 3%-30%; the R5, R6, R7 and R8
  • the imino group contained in is connected to the furoacetyl group of the reversibly substituted cyclohexenyl of formula I.
  • the R1, R2, R3 and R4 are independently selected from an alkyl group; one of the R1, R2, R3 and R4 is connected to the nitrogen atom of the reversibly substituted cyclohexenyl of formula I; preferably , the R5, R6, R7 and R8 are independently selected from imino substituted alkyl; the imino group of one of the R5, R6, R7 and R8 and the furoacetyl of the reversibly substituted cyclohexenyl of formula I connect.
  • the carbon chain parts in R1, R2, R3, R4 and R5, R6, R7 and R8 are independently selected from one of C1-C5 alkyl groups.
  • R2 and R6 are respectively propyl and imino substituted propyl or the molecular formula shown in formula VI, and the R3, R4, R5, R7 and R8 are respectively methyl;
  • n3 and n3 are respectively selected from integers not less than 1, specifically, m3 is 2, and n3 is 3.
  • aminated polysiloxane is based on aminodialkoxysilane coupling agent, dimethyldialkoxysilane and hexamethyldisiloxane hydrolysis, capping preparation, amino grafting
  • the calculation of the rate is according to the NMR method, by calculating the ratio of the amino peak area to the Si-CH3 peak area:
  • Grafting rate 3*amino peak area/2*Si-CH3 peak area*100%.
  • the ratio between the m1 value and the m2 value is 1:1.5, so as to ensure that the Diels-Alder reaction can proceed completely.
  • the modified polysiloxane A and the modified polysiloxane B are linear polysiloxanes respectively, which increases the flexibility and film-forming properties of the obtained organosilicon polymer material.
  • a method for preparing a self-healing silicone polymer material includes the following steps:
  • modified polysiloxane A is polysiloxane A having at least one maleimide group substitution in one molecule;
  • modified polysiloxane B said modified polysiloxane B is polysiloxane B having at least one furoacetyl group substitution in one molecule;
  • modified polysiloxane A and modified polysiloxane B are dissolved and then heated to cause a Diels-Alder reaction to generate the organosilicon polymer material crosslinked by at least one reversibly substituted cyclohexene.
  • the preparation method of the modified polysiloxane A comprises the following steps:
  • Aminated polysiloxane A is provided;
  • the modified polysiloxane A is obtained by dissolving the aminated polysiloxane A and maleic anhydride in the organic solvent I and heating to reflux for at least 3 hours.
  • the molecular weight of the aminated polysiloxane A is 2000-20000; and the grafting rate of the amino groups in the aminated polysiloxane A is 3%-30%, and the amino groups in the amino group
  • the molar ratio of polysiloxane A to the maleic anhydride is 1:1-3.
  • the weight-average molecular weight range of the aminated polysiloxane A is 2000-20000. Because the amino grafting rate is low, this molecular weight range can promote the free stretching of the molecular chain in a benign solvent, which is beneficial to the maleic anhydride and the side chain.
  • the amino group reacts to avoid the incomplete reaction caused by the inability of the molecular chain to stretch freely due to too large a molecular weight.
  • the grafting rate of amino groups in the aminated polysiloxane A is conducive to the grafting of maleimide functional groups with larger steric volumes, avoiding the steric hindrance between maleimide groups.
  • the response is incomplete.
  • the molar ratio of the amino group to the maleic anhydride is favorable for the sufficient reaction between the maleic anhydride and the amino group, avoiding the problem of incomplete reaction.
  • the upper and lower limits of the weight average molecular weight range of the aminated polysiloxane A can be selected from 3000, 5000, 8000, 11000, 14000, 17000 or 19000, respectively.
  • the weight average molecular weight may be 3000, 5000, 8000, 10000 or 15000.
  • the grafting rate of amino groups in the aminated polysiloxane A is 3%-30%. Furthermore, the grafting rate of amino groups in the aminated polysiloxane A is 10%-15%.
  • the molar ratio of the aminated polysiloxane A to the maleic anhydride in terms of amino groups is 1:1.5-2.5.
  • the organic solvent I is glacial acetic acid.
  • the heating reaction temperature is 140-180°C
  • the reflux reaction time is 4-8h, that is, the modified polysiloxane Alkane A.
  • the preparation method of the modified polysiloxane B comprises the following steps:
  • Aminated polysiloxane B is provided;
  • the molecular weight of the aminated polysiloxane B is 2000-20000;
  • the grafting rate of the amino group in the aminated polysiloxane B is 3%-30%, and the molar ratio of the amino group to the furoacetyl chloride is 1:1-5; the acid-binding agent and the The mass ratio of aminated polysiloxane B is 3wt%-7wt%.
  • the weight-average molecular weight range of the aminated polysiloxane B is beneficial to the reaction between furoacetyl chloride and the amino side chain in the aminated polysiloxane, and avoids incomplete reaction.
  • the grafting ratio of amino groups in the aminated polysiloxane B is beneficial to the dispersed distribution of amino side chains on the polysiloxane main chain, and avoids the problem of incomplete reaction caused by too concentrated dispersion.
  • the molar ratio of the amino group to the furoyl chloride is conducive to the completeness of the reaction between the furoyl chloride and the side chain amino group, and avoids incomplete reaction.
  • the mass ratio of the acid-binding agent to the aminated polysiloxane B is conducive to the timely adsorption of hydrogen chloride produced by the reaction of acid chlorides and amino groups, and avoids the breakage of polysiloxane chains caused by excessive acidity.
  • the upper limit and the lower limit of the range of the weight average molecular weight of the aminated polysiloxane B can be selected from 3000, 5000, 8000, 11000, 14000, 17000 or 19000 respectively, the specific aminated polysiloxane B
  • the weight average molecular weight may be 3000, 5000, 8000, 10000 or 15000.
  • the grafting rate of amino groups in the aminated polysiloxane B is 3%-30%. Furthermore, the grafting rate of amino groups in the aminated polysiloxane B is 10%-15%.
  • the molar ratio of the aminated polysiloxane B to the furoacetyl chloride in terms of amino groups is 1:1-1.5.
  • the mass ratio of the acid-binding agent to the aminated polysiloxane B is 4wt%-6wt%.
  • the acid-binding agent is at least one selected from pyridine, triethylamine, 4-dimethylaminopyridine, potassium carbonate, sodium carbonate and cesium carbonate. More preferably, the acid-binding agent is pyridines.
  • the organic solvent II is at least one selected from anhydrous ether, tetrahydrofuran and dichloromethane.
  • the modified polysiloxane A and modified polysiloxane B are dissolved in the organic solvent III and reacted at a temperature of 150°C-200°C for at least 15h, preferably 24h-48h, to ensure the reaction yield It can reach more than 95%.
  • the molar ratio of modified polysiloxane A based on maleimide group to modified polysiloxane B based on furoacetyl group is 1:1-4.
  • the molar ratio of the modified polysiloxane A based on maleimide groups to the modified polysiloxane B based on furoacetyl groups is 1:2-3.
  • the organic solvent III is selected from one of dimethyl ether, xylene, benzyl alcohol, dicarboxylate and ethyl benzoate.
  • the fertilizer particles in the coating machine are further controlled to present a continuous material curtain, so that the organosilicon polymer material can be directly sprayed on the surface of the suspended fertilizer particles and form a film before falling into the coating.
  • the inner wall of the clothing machine it is more conducive to the uniformity of film formation.
  • controlling the temperature to make the surface of the fertilizer micro-melt is conducive to better adhesion and bonding of the fertilizer surface and the organic silicon polymer material.
  • the coating machine rotates at a speed of 40-80r/m.
  • the rotating speed of the coating machine is 50-70r/m.
  • the control of the rotation speed can prevent the coated fertilizers from sticking to each other.
  • the mass ratio of the organosilicon polymer material to the fertilizer granules is 1%-8%.
  • the temperature of the preheated fertilizer granules is 80-140°C.
  • the temperature of the preheated fertilizer granules is 90-110°C.
  • the fertilizer preferably applicable to the preheating temperature is urea.
  • the coated organosilicon polymer material used in the slow-release coated fertilizer can realize the breaking and cross-linking of cross-linked bonds at a specific temperature, and can be used as a fertilizer coating material , using the temperature reversibility of the Diels-Alder reaction, the bonding and dissociation characteristics of chemical bonds can be controlled by temperature. If the coating is uneven, the coating treatment can be repeated many times, reducing the defective rate and improving the coating quality. The yield rate is high, and the problem of poor fertilizer slow-release effect caused by uneven coating is avoided.
  • the Si-O segment of the coated organic silicon material in the slow-release coated fertilizer has extremely strong hydrophobic properties
  • the maleimide group and furan acetylation The reversible cross-linking of the group provides holes inside the composite material, which ensures the slow-release effect of the coated fertilizer.
  • the slow-release coated fertilizer of the present application can realize industrialization and has huge economic value and industry influence; it is green and environmentally friendly, and can realize "recycling of polymer materials” and has huge potential develop potential.
  • the film formed by the coating is uniform, the fertilizer particles and the film are well bonded, and the process can be repeated to repair the uneven coating produced, so as to avoid solving the problem caused by the coating. Non-uniformity produces waste.
  • the coated organosilicon polymer material used in the slow-release coated fertilizer is a mixture of maleimide functionalization and furan acetylated polysiloxane. Constructed by catalyst-type Diels-Alder reaction, there is no problem of catalyst removal and residue, and the post-treatment steps are simple.
  • Fig. 1 (A) and (B) are respectively the infrared spectrograms of maleimidated polysiloxane A1# and furan acetylated polysiloxane B1# involved in Example 1 of the present application;
  • Fig. 2 (A) and (B) are respectively embodiment 1 and maleimidated polysiloxane A1#, furan acetylated polysiloxane B1# GPC spectrogram;
  • Fig. 3 (A) is the thermogravimetric analysis figure of organosilicon polymer material 1# under nitrogen and air; (B) is the DSC spectrogram of organosilicon polymer material 1#;
  • Fig. 4 is the microstructure schematic diagram of the organosilicon polymer material 1# obtained in embodiment 1;
  • Fig. 5 is the optical performance spectrogram of the organosilicon polymer material 1# obtained in embodiment 1, (A) is the ultraviolet spectrum and (B) is the fluorescence spectrogram;
  • Fig. 6 (A) is the urea granule figure that embodiment 2 uses; (B) is the coated fertilizer 1# photograph behind the organosilicon polymeric material 1# coated urea granule;
  • Fig. 7 is the coated fertilizer 1#-3# slow-release property spectrogram that embodiment 2,4,6 makes respectively in 60d;
  • Fig. 8 is the self-repair diagram of the organosilicon compound fertilizer obtained in Example 2, (A) the 1# shell of the organosilicon polymer material after urea release; (B) the 2# shell of the organosilicon polymer material after the Diels-Alder reverse reaction repair occurred .
  • Fig. 9 is a schematic diagram of the process and structure of the preparation of the organosilicon polymer material in the embodiment.
  • Hydrocharbyl includes alkyl, alkenyl, alkynyl and aryl.
  • Alkyl means a monovalent aliphatic hydrocarbon group.
  • An alkyl group can have any number of carbon atoms.
  • Many alkyl groups are C1 to C30.
  • Some alkyl groups can be C1 or larger, such as C2 or larger, C4 or larger, C6 or larger, or C8 or larger.
  • Some alkyl groups can be C22 or less, C16 or less, C12 or less, C8 or less, or C4 or less.
  • any alkyl groups may independently be linear, branched, cyclic, or combinations thereof (eg, cyclic alkyl groups may also have linear or branched components.)
  • Exemplary Alkyl includes methyl, ethyl, propyl, isopropyl, n-butyl, tert-butyl, sec-butyl, isobutyl, 2-ethylhexyl, isooctyl, dodecyl, hexadecane base, docosyl group and so on.
  • Aryl refers to a monovalent aromatic group.
  • Aryl groups may include only carbon and hydrogen, or may also include one or more heteroatoms, such as one or more of oxygen, nitrogen, and sulfur.
  • Aryl groups can have an aromatic ring with three or more atoms, four or more atoms, or five or more atoms.
  • Aryl groups can have rings with ten or fewer atoms, eight or fewer atoms, seven or fewer atoms, or six or fewer atoms.
  • Exemplary aryl groups include phenyl, furyl, naphthyl, anthracenyl, and the like. Phenyl is a common aryl substituent.
  • Amino means a group having the formula -Nc(H)p(R')q, wherein each R' is independently an alkyl, alkenyl, alkynyl, aryl, or alkaryl group, any of which One may be optionally substituted, p+q is 2 or 3, and c represents the charge on the nitrogen atom, which is 0 or 1+. Typically, each R' is an alkyl group. When p+q is 2, c is 0; when p+q is 3, c is 1+.
  • the amino group can be primary, secondary, tertiary or quaternary, depending on the value of q. Amino groups with q values of 0, 1, 2 and 3 are primary, secondary, tertiary and quaternary ammonia, respectively.
  • Polydiorganosiloxane refers to a polymer having the repeating unit -Si(G) 2O- , wherein each occurrence of G is independently an organic moiety.
  • G is typically independently alkyl, aryl, alkenyl or alkynyl. Alkyl and aryl are the most common, and alkyl is more common than aryl.
  • G is aryl, it may be any aryl group, for example any group referred to herein by the definition of "aryl”. Typical aryl groups include phenyl.
  • Typical alkyl groups include those discussed with reference to the definition of alkyl herein, and also include C1 to C22 alkyl, C1 to C16 alkyl, C1 to C12 alkyl, C1 to C8 alkyl, or C1 to C4 Alkyl groups such as methyl, ethyl, propyl, butyl (such as tert-butyl, isobutyl, n-butyl and sec-butyl), and C8 alkyl groups such as 2-ethylhexyl and isooctyl.
  • the end groups of polydiorganosiloxanes can vary; typical end groups include triorganosilyl groups and hydroxyl groups, as well as capping, quenching, and chain transfer groups .
  • the raw materials, reagents and fertilizers in the examples of the present application were purchased through commercial channels.
  • the raw material aminated polysiloxane is self-made in the laboratory, using aminopropylmethyldiethoxysilane or 3-(2-aminoethyl)-aminopropylmethyldiethoxysilane and dimethyl Side aminopolysiloxane prepared by hydrolysis of diethoxysilane, prepared by hydrolysis of aminopropyldimethylethoxysilane or 3-(2-aminoethyl)-aminopropyldimethylethoxysilane become.
  • the test method is the method of soaking in water, leaching the coating with water or a certain concentration of salt solution Controlled-release fertilizers to calculate the amount of nutrients dissolved within a certain period of time.
  • the figure shows the process of reversible reaction and thermal self-repair, and the structure diagram of the obtained organosilicon composite material, in which, 1 is the Si-O-Si segment in polysiloxane, and 2 is maleyl Imino group, 3 is furoacetyl, 4 is
  • the preparation method of self-healing silicone polymer material comprises the following steps:
  • Step 1 preparation of modified polysiloxane A (maleimidated polysiloxane A): Amine-terminated polysiloxane A or Side aminated polysiloxane A and maleic anhydride were placed in a 100mL round-bottomed flask equipped with an air duct, a constant pressure low liquid funnel and a spherical condenser, heated to 140-180°C under electromagnetic stirring and refluxed to react 4- After 8 hours, remove glacial acetic acid under reduced pressure and dissolve the residue with chloroform, purify and wash with saturated sodium chloride aqueous solution several times and separate the organic phase; add anhydrous magnesium sulfate to the organic phase and dry overnight, remove the organic solvent under reduced pressure to obtain a brown transparent oil Liquid, that is, the modified polysiloxane A is obtained;
  • the weight average molecular weight of aminated polysiloxane A includes but not limited to 3000, 5000, 10000, 15000, the grafting ratio of amino groups in aminated polysiloxane A includes but not limited to 3%-30%.
  • the molar ratio of maleic anhydride is 1:1-1:3;
  • Step 2 Preparation of modified polysiloxane B (furan acetylated polysiloxane B): Three extractions and three discharges were performed on a 50mL round bottom flask, and then nitrogen was introduced for protection. Terminal amino-modified polysiloxane B or pendant amino-modified polysiloxane B, dissolved in 20mL organic solvent II, and introduced acid-binding agent, the amount of acid-binding agent added is amino-modified polysiloxane B 3%-7% of the mass; after electromagnetic stirring for 15-30min, slowly drop the furoyl chloride dissolved in the organic solvent II into the round bottom flask, the molar ratio of amino group to furoyl chloride is 1:1-1:1.5 , and reacted for 1h-3h under reflux; vacuum distillation and purification were performed to remove the generated salt by suction filtration to obtain a light yellow oily liquid, which was to obtain modified polysiloxane B;
  • the weight-average molecular weight of amino-modified polysiloxane B includes but is not limited to 3000, 5000, 10000, and 15000, and the amino graft ratio of amino-modified polysiloxane B includes but is not limited to 3%-30%.
  • Solvent II includes but not limited to anhydrous ether, tetrahydrofuran, dichloromethane; acid-binding agents include but not limited to pyridine, triethylamine, 4-dimethylaminopyridine, potassium carbonate, sodium carbonate, cesium carbonate, etc.; organic solvents
  • the volume of furoacetyl chloride in II: the volume (v:v) ratio is 1:5-1:10;
  • Step 3 preparation of silicone polymer material: Dissolve modified polysiloxane A (maleimidated polysiloxane A) and modified polysiloxane B (furan acetylated polysiloxane B) in After the organic solvent III, transfer to a round bottom flask, heat to 150°C-200°C under electromagnetic stirring and react for 24h-48h; after the reaction is completed, pour it into anhydrous methanol solution to obtain a light red precipitate, remove the organic solvent by suction filtration After III, repeatedly wash with anhydrous methanol for several times, and vacuum dry overnight to obtain the organosilicon polymer material;
  • organic solvent III includes but not limited to dimethyl ether, xylene, benzyl alcohol, diformic acid ester, ethyl benzoate Esters etc.
  • the application of the self-healing organosilicon polymer material as a fertilizer coating includes the following steps:
  • Organosilicon polymer material as fertilizer coating process After sieving the fertilizer with sieves of different meshes (10-40 mesh), divide the fertilizer into 50g portions;
  • reaction equations of modified polysiloxane A1# and modified polysiloxane B1# of the present embodiment are as follows respectively
  • the preparation method of self-healing organosilicon polymer material 1# comprises the following steps:
  • modified polysiloxane A1# maleimidated polysiloxane A1#: Aminopropyl-terminated polysiloxane with a weight-average molecular weight of 5000 dispersed in 30 mL of glacial acetic acid Alkanes and maleic anhydride are placed in a 100mL round-bottomed flask equipped with an airway tube, a constant pressure low liquid funnel and a spherical condenser at a molar ratio of amino to maleic anhydride of 1:1, and heated to 140°C under electromagnetic stirring After reflux for 4 hours, the glacial acetic acid was removed under reduced pressure and the residue was dissolved in chloroform, purified and washed several times with saturated aqueous sodium chloride solution, and the organic phase was separated.
  • Modified polysiloxane B1# furan acetylated polysiloxane B1#: the 50mL round-bottomed flask was pumped three times and vented three times, and then passed into nitrogen for protection.
  • the modified polysiloxane A and The Diels-Alder reaction between the modified polysiloxane B is more complete, and the performance of the obtained film is better, and the selected aminopropyl polysiloxane is the same as that selected in A1#.
  • thermogravimetric analysis of organosilicon polymer material 1# under nitrogen and air is shown in Figure 3(A)
  • DSC spectrum of organosilicon polymer material 1# is shown in Figure 3(B)
  • schematic diagram of the microstructure of organosilicon polymer material 1# is shown in Figure 4 .
  • the ultraviolet spectrum of organosilicon composite material 1# is shown in Figure 5(A) and the fluorescence spectrum is shown in Figure 5(B).
  • organosilicon polymeric material 1# of embodiment 1# as the fertilizer coating process: after sieving the urea with a 10-mesh sieve, pack it with 50g as a portion; get a portion of urea in a drum coating machine, adjust The angle of the coating machine is 35°, and the speed is controlled at 40r/m, so that the urea can form a continuous material curtain in the coating machine; preheat after 15 minutes, and the temperature is controlled at about 90°C, so that the surface of the urea particles is in a slightly molten state , spray into the organosilicon polymer material 1# dissolved in dichloromethane solution, the addition amount of the organosilicon polymer material 1# is selected as 1% of the fertilizer mass, and the rotation speed is adjusted during the coating process to prevent mutual adhesion, so that the organosilicon polymerizes Material 1# forms a uniform film on the surface of urea granules to obtain coated fertilizer 1#.
  • Fig. 6(A) is a photo of urea granules
  • Fig. 6(B) is a photo of coated fertilizer 1#.
  • the preparation method of self-repairing organosilicon polymer material 2# comprises the following steps:
  • modified polysiloxane A2# maleimidated polysiloxane A2#
  • the side aminopropyl modified polysiloxane with a weight average molecular weight of 5000 dispersed in 30mL of glacial acetic acid Alkanes and maleic anhydride are placed in the 100mL round-bottomed flask that airway is housed with amino group and maleic anhydride mol ratio as 1:3, amino graft rate 15%, constant pressure low liquid funnel and spherical condenser, in After heating to 160°C under electromagnetic stirring and reflux for 6 hours, the glacial acetic acid was removed under reduced pressure and the residue was dissolved with chloroform, purified and washed several times with saturated aqueous sodium chloride solution, and the organic phase was separated.
  • Modified polysiloxane B2# (furan acetylated polysiloxane B2#): the 50mL round-bottomed flask was pumped three times and discharged three times, and then passed through nitrogen for protection.
  • the side aminopropyl group with a weight average molecular weight of 5000 The modified polysiloxane was dissolved in 20mL of anhydrous ether, the grafting rate of amino group was 15%, and the acid-binding agent triethylamine was added, and the amount of triethylamine added was 5% of the mass of the side aminopropyl modified polysiloxane ; After electromagnetic stirring for 20min, the furoyl chloride dissolved in the organic solvent tetrahydrofuran was slowly dropped into the round-bottomed flask with a volume to mass ratio (mL:g) of 15:1, wherein the molar ratio of amino group to furoyl chloride was 1 :3, after reacting for 2h under the reflux state,
  • organosilicon polymer material 2# Maleimidated polysiloxane A2# and furanacetylated polysiloxane B2# were calculated by maleimide group and furanacetyl group in a molar ratio of 1:2.5 was dissolved in the organic solvent xylene, the volume-to-mass ratio (mL:g) between the solvent and the raw material was 25:1, and transferred into a round bottom flask, heated to 180°C under electromagnetic stirring and reacted for 36h, Then pour it into anhydrous methanol solution to obtain a light red precipitate, remove the solvent by suction filtration, wash with anhydrous methanol several times, and vacuum dry overnight to obtain organosilicon polymer material 2#.
  • mL:g volume-to-mass ratio
  • organosilicon polymeric material 2# of embodiment 3# as the fertilizer coating process: after the urea is sieved with a 39-purpose sieve, it is divided into parts with 50g; get a part of urea in a drum coating machine, adjust The angle of the coating machine is 40°, and the speed is controlled at 60r/m, so that the urea can form a continuous material curtain in the coating machine; preheat after 15 minutes, and the temperature is controlled at about 100°C, so that the surface of the urea particles is in a slightly molten state , spray into the organosilicon polymer material 2# dissolved in dichloromethane solution, the addition amount of the organosilicon polymer material 2# is selected as 1.5% of the fertilizer mass, and the rotation speed is adjusted during the coating process to prevent mutual adhesion, so that the organosilicon polymerizes Material 1# forms a uniform film on the surface of urea granules.
  • the preparation method of the organic silicon polymer material 3# of self-healing comprises the following steps:
  • modified polysiloxane A3# maleimidated polysiloxane A3#: The side aminopropyl modified polysiloxane with a weight average molecular weight of 15000 dispersed in 30mL of glacial acetic acid Alkane and maleic anhydride are placed in the 100mL round-bottomed flask of constant pressure low liquid funnel and spherical condenser with airway tube being housed in the amount of 1:2.5 with amino group and maleic anhydride mol ratio, amino grafting rate 30%.
  • Modified polysiloxane B3# (furan acetylated polysiloxane B3#): the 50mL round-bottomed flask was pumped three times and released three times, and then passed through nitrogen for protection.
  • the side aminopropyl group with a weight average molecular weight of 15000 The modified polysiloxane was dissolved in 20mL of anhydrous ether, the grafting rate of the amino group was 30%, and the acid-binding agent 4-dimethylaminopyridine was added, and the amount of 4-dimethylaminopyridine added was the 5% of the quality of oxane B3#; after electromagnetic stirring for 30min, the furoyl chloride dissolved in the organic solvent methylene chloride of 30:1 was slowly dropped into the round-bottomed flask with a volume to mass ratio (mL:g), The molar ratio of amino group to furoacetyl chloride is 1:5. After reacting under reflux for 3 hours, remove the generated salt
  • organosilicon polymer material 3# Maleimidated polysiloxane A3# and furanacetylated polysiloxane B3# were calculated by maleimide group and furanacetyl group in molar ratio of 1:3 dissolved in the organic solvent benzyl alcohol, the volume-to-mass ratio between the solvent and the raw material (mL:g) is 30:1, and transferred to a round bottom flask, heated to 200°C under electromagnetic stirring and reacted for 48h , and then poured into anhydrous methanol solution to obtain a light red precipitate. After the solvent was removed by suction filtration, it was repeatedly washed with anhydrous methanol several times, and vacuum-dried overnight to obtain organosilicon polymer material 3#.
  • organosilicon polymer material 3# of embodiment 5# as the fertilizer coating process: after the urea is sieved with a 40-mesh sieve, 50g is used as a portion to pack respectively; get a portion of urea in a drum coating machine, adjust The angle of the coating machine is 45°, and the speed is controlled at 80r/m, so that the urea can form a continuous material curtain in the coating machine; preheat after 15 minutes, and the temperature is controlled at about 110°C, so that the surface of the urea particles is in a slightly molten state , spray into the organosilicon polymer material 3# dissolved in dichloromethane solution, the addition amount of the organosilicon polymer material 3# is selected as 2% of the fertilizer mass, and the rotation speed is adjusted during the coating process to prevent mutual adhesion, so that the organosilicon polymerizes Material 3# forms a uniform film on the surface of urea granules.
  • Example 7 The slow-release performance test of coated fertilizer 1-3#
  • Example 3 has a better slow-release effect than 1 and 2, and the cumulative release rate within 28 days has not exceeded 80%, which has met the requirements of slow-release fertilizers.
  • the coated fertilizer prepared by the present application has a slow slow release rate, can maintain nutrients and can be fully absorbed by crops, has a low fertilizer loss rate, and greatly improves the fertilizer utilization rate, thereby avoiding excessive application of fertilizers.
  • the prepared coated fertilizers 1#, 2# and 3# did not exceed 80% of the cumulative nitrogen release rate in 28 days, which has reached the requirements of GB/T 23348-2009, and the coated fertilizer 3# accumulated nitrogen in 28 days
  • the release rate is lower than 1#, 2# and commercially available products, indicating that the slow-release effect of coated fertilizer 3# is better.
  • Fig. 8(A) is the shell surface of the organosilicon composite material after the nutrient release of the prepared coated fertilizer 1#. It can be seen from Fig. 8(A) that the organosilicon composite material can form a shell with holes on the surface of the fertilizer, but as the nutrients After release, the surface may collapse and create debris around it.
  • Figure 8(B) shows the 2# shell of the organic silicon composite material repaired by the Diels-Alder reverse reaction after the conditioned treatment of the coated fertilizer 3# material.
  • coated fertilizers 4#-10# and contrast coated materials D1#-D2# were respectively tested using the test method of Example 7
  • the 28-day cumulative nitrogen release rate and the repairable times of the coating material are shown in Table 2.
  • Coated fertilizer 11#- and contrast coated material D2#- were prepared respectively according to the conditions different from the method in Example 1 and Example 2 in Table 3, and the test method of Example 7 was used to test the accumulated nitrogen in 28 days respectively Table 3 shows the release rate of the hormone and the number of times the coating material can be repaired.
  • the rotation speed of the material curtain in the coating machine is fast, and the curing time of the coating material on the surface of the fertilizer is short.
  • the coating material is easy to fall off from the surface of the fertilizer or create gaps, resulting in poor slow-release effect.
  • the coating efficiency is low because the speed is too slow; compared with the coated fertilizer D5#, with the mass ratio of the organic silicon polymer material to the fertilizer particle On the one hand, it can increase the viscosity of the coating liquid, so that its adhesion on the surface of the fertilizer can be increased; Reduce the 28-day cumulative nitrogen release rate, but the European Standards Committee pointed out in the relevant regulations on slow-release fertilizers: within the specified time, the nutrient release rate of slow-release fertilizers should not be less than 75%, although the 28-day accumulation of coated fertilizer D5# The nitrogen release rate is lower than that of the examples, but the low release rate causes the fertilizer to fail to provide sufficient nutrients for the crops within the specified time and does not meet the slow-release fertilizer standard, so it cannot be put into the slow-release fertilizer market for use.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Pest Control & Pesticides (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Soil Sciences (AREA)
  • Fertilizers (AREA)

Abstract

A slow-release coated fertilizer and a preparation method therefor, belonging to the field of composite materials. The slow-release coated fertilizer comprises a fertilizer particle and a thin film coated outside the fertilizer particle. The thin film is prepared from a silicone polymeric material, wherein the silicone polymeric material is prepared by a Diels-Alder reaction between a modified polysiloxane A and a modified polysiloxane B. The organopolysiloxane A has at least one non-aromatic conjugated diene bond in one molecule, and the organopolysiloxane B has at least one substituted olefinic bond which is subjected to the Diels-Alder reaction with the non-aromatic conjugated diene bond in one molecule. The slow-release coated fertilizer has a high coating uniformity, which is beneficial for the slow release of the fertilizer and gives a good slow-release effect; and the thin film of the slow-release coated fertilizer has a good hydrophobic property, permeability, film-forming property and reusability, so that the slow-release coated fertilizer uses a small amount of coating material, has significant advantages and has a positive effect on environmental protection.

Description

[根据细则37.2由ISA制定的发明名称] 缓释包膜肥料及其制备方法[Title of the invention established by the ISA under Rule 37.2] Slow-release coated fertilizers and processes for their preparation 技术领域technical field
本申请涉及一种缓释包膜肥料及其制备方法,属于肥料制备领域。The application relates to a slow-release coated fertilizer and a preparation method thereof, belonging to the field of fertilizer preparation.
背景技术Background technique
随着世界人口的急速增长及人民生活水平的逐步提高,对粮食的产量和品质的需求逐年增加,肥料的施用成为当今提高粮食品质和产量最行之有效的方法。伴随着农业的快速发展,农业生产中过度施用肥料的现象屡见不鲜,究其原因是肥料施加后因受到雨水冲刷、光照分解等外界因素影响,大部分养分在被农作物吸收前已流失,使肥料利用率大大降低,从而导致过度施用肥料现象。而过度施用肥料会对农作物生长产生抑制、使农产品品质下降、导致土壤结构破坏及面源污染等。因此如何在保证粮食高产稳产的前提下提高肥料利用率,进而降低农业生产成本,减轻农业增速发展所带来的面源污染,实现农业的绿色生态可持续发展,成为当前我国乃至世界农业发展研究的重点问题。With the rapid growth of the world's population and the gradual improvement of people's living standards, the demand for grain production and quality is increasing year by year. The application of fertilizers has become the most effective method to improve grain quality and production. With the rapid development of agriculture, the phenomenon of excessive application of fertilizers in agricultural production is not uncommon. The reason is that after the application of fertilizers, due to the impact of external factors such as rain erosion and light decomposition, most of the nutrients have been lost before being absorbed by crops. The rate is greatly reduced, which leads to the phenomenon of over-application of fertilizer. Excessive application of fertilizers will inhibit the growth of crops, reduce the quality of agricultural products, lead to soil structure damage and non-point source pollution. Therefore, how to improve the utilization rate of fertilizers on the premise of ensuring high and stable grain production, thereby reducing agricultural production costs, reducing non-point source pollution caused by agricultural growth and development, and realizing the sustainable development of agricultural green ecology has become the current agricultural development in my country and the world. Key questions of the research.
有机硅高分子材料作为一类特殊的高分子材料,其特有的Si-O链段使其在热性能、柔性、成膜性、疏水性等方面展现出特有的优势。前期研究结果表明,有机硅高分子可在基质表面形成致密的保护膜,在强酸、强碱的作用下仍可防止其对基质的腐蚀,且疏水性极佳,上述研究结果表明有机硅高分子可作为疏水涂层用于肥料的缓释。但有机硅高分子制备过程中多需要Pt催化剂作用,成本相对较高,阻碍了有机硅高分子在农业领域的应用。另一方面,现有缓释肥料因包膜材料性能差导致的因缓释效果不佳,而引起资源浪费和肥料滥施滥用的问题。Silicone polymer materials are a special class of polymer materials, and their unique Si-O segments make them exhibit unique advantages in terms of thermal properties, flexibility, film-forming properties, and hydrophobicity. Previous research results show that organosilicon polymers can form a dense protective film on the surface of the substrate, which can still prevent corrosion of the substrate under the action of strong acids and alkalis, and have excellent hydrophobicity. The above research results show that organosilicon polymers Can be used as a hydrophobic coating for slow release of fertilizers. However, the Pt catalyst is often required in the preparation process of organosilicon polymers, and the cost is relatively high, which hinders the application of organosilicon polymers in the agricultural field. On the other hand, the slow-release effect of existing slow-release fertilizers is poor due to the poor performance of the coating material, which causes the problems of waste of resources and indiscriminate application of fertilizers.
发明内容Contents of the invention
为解决上述问题,本申请提供了一种缓释包膜肥料及其制备方法,该缓释包膜肥料的包膜的均匀性高,有利于肥料的缓释,缓释效果好;缓释包膜肥料外层的包膜材料疏水特性、通透性、成膜性及可重复利用好,故缓释包膜肥料使用的包膜材料量低具有显著优势,对保护环境具有积极的作用;缓释包膜肥料的加工成本低。In order to solve the above problems, the application provides a slow-release coated fertilizer and a preparation method thereof. The uniformity of the coating of the slow-release coated fertilizer is high, which is beneficial to the slow-release of the fertilizer, and the slow-release effect is good; the slow-release package The coating material of the outer layer of the film fertilizer has good hydrophobicity, permeability, film-forming property and reusability, so the low amount of coating material used in the slow-release coated fertilizer has a significant advantage and has a positive effect on protecting the environment; The processing cost of release coated fertilizer is low.
根据本申请的一个方面,提供了一种缓释包膜肥料,其包括肥料颗粒和包覆在所述肥料颗粒外的薄膜,所述薄膜由有机硅聚合材料制得;According to one aspect of the present application, a slow-release coated fertilizer is provided, which includes fertilizer granules and a film coated outside the fertilizer granules, and the film is made of a silicone polymer material;
其中,有机硅聚合材料由所述改性聚硅氧烷A和改性聚硅氧烷B发生Diels-Alder反应制得,所述有机聚硅氧烷A在1分子中具有至少一个包含取代烯烃键基团,所述有机聚硅氧烷B在1分子至少具有一个与所述包含取代烯烃键基团发生Diels-Alder反应的包含非芳烃的共轭双烯键基团。Wherein, the organosilicon polymer material is prepared by the Diels-Alder reaction of the modified polysiloxane A and the modified polysiloxane B, and the organopolysiloxane A has at least one substituted olefin in one molecule. The organopolysiloxane B has at least one non-aromatic conjugated diene bond group that undergoes a Diels-Alder reaction with the substituted olefin bond group in one molecule.
有机聚硅氧烷中的Si-O链段使其在热性能、柔性、成膜性、疏水性等方面展现出特有的优势,并且有机聚硅氧烷在肥料表面形成致密的保护膜,在强酸、强碱的作用下仍可防止其对肥料的腐蚀,且疏水性极佳,具有作为肥料包膜的优异特性;并且本申请通过具有Diels-Alder反应直接制得有机聚硅氧烷不仅降低了肥料的包膜成本,并且控制制得的有机聚硅氧烷的孔隙率既可以保证肥料释放,且释放的速率比较缓慢有利于植物充分吸收肥料养分,提高肥料的利用率;并且有机聚硅氧烷可以发生Diels-Alder反应从而可以实现重复包膜来提供形成的薄膜的均匀性,以避免由于包膜不均匀而造成的肥料释放不均匀的问题。The Si-O segment in organopolysiloxane makes it exhibit unique advantages in terms of thermal performance, flexibility, film-forming property, hydrophobicity, etc., and organopolysiloxane forms a dense protective film on the surface of the fertilizer. Under the action of strong acid and strong alkali, it can still prevent its corrosion to fertilizers, and has excellent hydrophobicity, and has excellent characteristics as a fertilizer coating; The coating cost of the fertilizer is reduced, and the porosity of the prepared organopolysiloxane can ensure the release of the fertilizer, and the release rate is relatively slow, which is conducive to the plant to fully absorb the fertilizer nutrients and improve the utilization rate of the fertilizer; and the organopolysiloxane Oxane can undergo Diels-Alder reaction so that repeated coating can be achieved to provide uniformity of the formed film, so as to avoid the problem of uneven fertilizer release caused by uneven coating.
可选地,所述有机硅聚合材料与所述肥料颗粒的质量比为0.3%-5%。可选地,所述有机硅聚合材料与所述肥料颗粒的质量比的上、下限分别独立的选自0.5%、1%、2%、3%或4%。选自0.5%-5%。优选地,所述有机硅聚合材料与所述肥料颗粒的质量比为0.3%-3%,更优选为1%-3%。该质量比的控制既能保证肥料包膜的完整性,又能减少包膜材料的使用量,同时有利于控制肥料的释放速率最佳。Optionally, the mass ratio of the organosilicon polymer material to the fertilizer granules is 0.3%-5%. Optionally, the upper and lower limits of the mass ratio of the organosilicon polymer material to the fertilizer granules are independently selected from 0.5%, 1%, 2%, 3% or 4%. Selected from 0.5%-5%. Preferably, the mass ratio of the organosilicon polymer material to the fertilizer particles is 0.3%-3%, more preferably 1%-3%. The control of the mass ratio can not only ensure the integrity of the fertilizer coating, but also reduce the usage of coating materials, and at the same time help to control the optimal release rate of the fertilizer.
可选地,所述肥料颗粒的粒径为10~40目。优选地,所述肥料颗粒的粒径为20~30目。该肥料颗粒的目数可以使得肥料可以在合适的时间内充分释放,过大会导致在有限的时间内养分不能完全释放,最终使肥料利用率降低;过小会导致肥料在未达到28天时已经完全释放,达不到缓释肥标准。Optionally, the particle size of the fertilizer particles is 10-40 mesh. Preferably, the particle size of the fertilizer particles is 20-30 mesh. The mesh size of the fertilizer granules can make the fertilizer fully released in a suitable time. If it is too large, the nutrients cannot be fully released in a limited time, and finally the fertilizer utilization rate will be reduced; if it is too small, the fertilizer will be completely released before it reaches 28 days. Release, not up to the slow-release fertilizer standard.
可选地,所述肥料颗粒选自尿素、氮磷钾复合肥、磷酸二铵、中量元素肥、生物肥和有机肥中的至少一种。Optionally, the fertilizer particles are selected from at least one of urea, NPK compound fertilizer, diammonium phosphate, medium element fertilizer, biological fertilizer and organic fertilizer.
可选地,所述改性聚硅氧烷A中的包含取代烯烃键基团可以为马来酰亚胺基,所述有机聚硅氧烷B中的所述包含非芳烃的双烯键基团为呋喃乙酰基;可选地,所述改性聚硅氧烷A中的包含取代烯烃键基团可以为马来酰亚胺基衍生物,所述有机聚硅氧烷B中的所述包含非芳烃的双烯键基团为呋喃乙酰基衍生物。Optionally, the substituted olefin bond group in the modified polysiloxane A may be a maleimide group, and the non-aromatic dien bond group in the organopolysiloxane B The group is a furoyl group; alternatively, the group containing a substituted olefin bond in the modified polysiloxane A can be a maleimide derivative, and the group in the organopolysiloxane B Diethylenic groups containing non-aromatic hydrocarbons are furoacetyl derivatives.
可选地,所述改性聚硅氧烷A中的包含取代烯烃键基团为马来酰亚胺基,所述有机聚硅氧烷B中的所述包含非芳烃的双烯键基团为呋喃乙酰基;Optionally, the group containing a substituted olefin bond in the modified polysiloxane A is a maleimide group, and the group containing a non-aromatic double olefin bond in the organopolysiloxane B is furoacetyl;
所述改性聚硅氧烷A和改性聚硅氧烷B通过生成至少一个可逆取代环己烯基交联聚合制得所述有机硅聚合材料,所述可逆取代环己烯基的结构如式Ⅰ所示:The modified polysiloxane A and the modified polysiloxane B are cross-linked and polymerized to produce at least one reversible substituted cyclohexenyl group to obtain the silicone polymer material, and the structure of the reversible substituted cyclohexenyl group is as follows: Formula I shows:
Figure PCTCN2021117481-appb-000001
Figure PCTCN2021117481-appb-000001
可选地,所述改性聚硅氧烷A和所述改性聚硅氧烷B通过多个马来酰亚 胺基和呋喃乙酰基可逆交联聚合,从而使得制得的有机硅聚合材料为多孔材料,能够作为缓释包膜材料使用。Optionally, the modified polysiloxane A and the modified polysiloxane B are reversibly cross-linked and polymerized through multiple maleimide groups and furoacetyl groups, so that the obtained silicone polymer material It is a porous material and can be used as a sustained-release coating material.
可选地,所述改性聚硅氧烷A中的马来酰亚胺基的接枝率为X,所述改性聚硅氧烷B中的呋喃乙酰基的接枝率为Y,所述接枝率X与接枝率Y的比值为1:1.2-1.5。Optionally, the grafting rate of the maleimide group in the modified polysiloxane A is X, and the grafting rate of the furoacetyl group in the modified polysiloxane B is Y, so The ratio of the grafting rate X to the grafting rate Y is 1:1.2-1.5.
优选地,所述接枝率X与接枝率Y的比值为1:1.2-1.5;更优选地,所述接枝率X与接枝率Y比值为1:1.5,以使得接枝的马来酰亚胺基和呋喃乙酰的能充分反应,以提高接枝原料的利用率。Preferably, the ratio of the grafting rate X to the grafting rate Y is 1:1.2-1.5; more preferably, the ratio of the grafting rate X to the grafting rate Y is 1:1.5, so that the grafted horse The imide group and furoacetyl can fully react to improve the utilization rate of grafting raw materials.
具体的,所述接枝率X为8%-20%,接枝率Y为5%-25%;优选地,所述接枝率X为10%-20%,接枝率Y为12%-24%。接枝率X和接枝率Y的数值能够保证制得的有机硅聚合材料的缓释效果,尤其是作为肥料包膜的缓释效果。Specifically, the grafting rate X is 8%-20%, the grafting rate Y is 5%-25%; preferably, the grafting rate X is 10%-20%, and the grafting rate Y is 12% -twenty four%. The values of the grafting ratio X and the grafting ratio Y can ensure the slow-release effect of the prepared organosilicon polymer material, especially the slow-release effect as a fertilizer coating.
X、Y接枝率的计算按照以下方法进行:用分析天平准确称取约1.5g的改性聚硅氧烷于锥形瓶中,加进约20mL的四氢呋喃和甲苯溶解,然后加入0.1mol/L的盐酸溶液,充分摇5min后加入酚酞指示剂,用标定过的氢氧化钠标准溶液测定过量的酸,直到溶液变色。此外,再对盐酸溶液做一次空白样。按以下公式计算氨基浓度和X、Y的接枝率:The calculation of the grafting ratio of X and Y is carried out according to the following method: Accurately weigh about 1.5g of modified polysiloxane in a conical flask with an analytical balance, add about 20mL of tetrahydrofuran and toluene to dissolve, and then add 0.1mol/ L of hydrochloric acid solution, shake well for 5 minutes, add phenolphthalein indicator, measure the excess acid with calibrated sodium hydroxide standard solution, until the solution changes color. In addition, do a blank sample again for the hydrochloric acid solution. Calculate the amino group concentration and the grafting ratio of X and Y according to the following formula:
氨基浓度=(V 0-V)C NaOH/m; Amino concentration=(V 0 -V)C NaOH /m;
接枝率=(反应前氨基浓度-反应后氨基浓度)/反应前氨基浓度×100%Grafting rate=(amino group concentration before reaction-amino group concentration after reaction)/amino group concentration before reaction×100%
其中:V 0——滴定空白样消耗的氢氧化钠体积(mL); Among them: V 0 ——the volume of sodium hydroxide consumed for titrating the blank sample (mL);
V——滴定试样消耗的氢氧化钠体积(mL);V—the volume of sodium hydroxide consumed by the titration sample (mL);
C NaOH——标准氢氧化钠浓度(mol/L); C NaOH - standard sodium hydroxide concentration (mol/L);
m——试样质量(g)。m—sample mass (g).
可选地,所述聚硅氧烷A和所述聚硅氧烷B分别独立的选自聚(二有机硅氧烷)。Optionally, the polysiloxane A and the polysiloxane B are independently selected from poly(diorganosiloxanes).
可选地,所述聚硅氧烷A的结构式如式Ⅱ所示:Optionally, the polysiloxane A has a structural formula as shown in Formula II:
Figure PCTCN2021117481-appb-000002
Figure PCTCN2021117481-appb-000002
其中,R1、R2、R3和R4分别独立的选自烃基、取代烃基、杂芳基、取代杂芳基和非烃类取代基中的一种;m1、n1分别取自>0的整数,式Ⅱ的氨基化聚硅氧烷A的重均分子量为2000~20000,所述氨基化聚硅氧烷A中的氨基的接枝率为3%-30%;所述R 1、R 2、R 3和R 4中的至少一种与式Ⅰ的可逆取代环己烯基的马来酰亚胺基连接。 Among them, R1, R2, R3 and R4 are independently selected from one of hydrocarbon groups, substituted hydrocarbon groups, heteroaryl groups, substituted heteroaryl groups and non-hydrocarbon substituents; m1 and n1 are respectively taken from integers>0, the formula The weight-average molecular weight of the aminated polysiloxane A of II is 2000-20000, and the grafting rate of amino groups in the aminated polysiloxane A is 3%-30%; the R 1 , R 2 , R At least one of 3 and R 4 is linked to the maleimide group of the reversibly substituted cyclohexenyl of formula I.
可选地,所述聚硅氧烷B的结构式分别如式Ⅲ所示:Optionally, the structural formulas of the polysiloxane B are shown in formula III:
Figure PCTCN2021117481-appb-000003
Figure PCTCN2021117481-appb-000003
其中,R5、R6、R7和R8分别独立的选自烃基、取代烃基、杂芳基、取代杂芳基和非烃类取代基中的一种;m2、n2分别取自>0的整数,式Ⅲ的氨基化聚硅氧烷B的重均分子量为2000~20000,所述氨基化聚硅氧烷B中的氨基的接枝率为3%-30%;所述R5、R6、R7和R8中含有的亚氨基与式Ⅰ的可逆取代环己烯基的呋喃乙酰基相连接。Among them, R5, R6, R7 and R8 are independently selected from one of hydrocarbon groups, substituted hydrocarbon groups, heteroaryl groups, substituted heteroaryl groups and non-hydrocarbon substituents; m2 and n2 are respectively taken from integers>0, the formula The weight average molecular weight of the aminated polysiloxane B of III is 2,000 to 20,000, and the grafting rate of amino groups in the aminated polysiloxane B is 3%-30%; the R5, R6, R7 and R8 The imino group contained in is connected to the furoacetyl group of the reversibly substituted cyclohexenyl of formula I.
优选地,所述R1、R2、R3和R4分别独立的选自烷基;所述R1、R2、R3和R4中的一种与式Ⅰ的可逆取代环己烯基的氮原子连接;优选地,所述R5、R6、R7和R8分别独立的选自亚氨基取代烷基;所述R5、R6、R7和R8中的一种的亚氨基与式Ⅰ的可逆取代环己烯基的呋喃乙酰连接。Preferably, the R1, R2, R3 and R4 are independently selected from an alkyl group; one of the R1, R2, R3 and R4 is connected to the nitrogen atom of the reversibly substituted cyclohexenyl of formula I; preferably , the R5, R6, R7 and R8 are independently selected from imino substituted alkyl; the imino group of one of the R5, R6, R7 and R8 and the furoacetyl of the reversibly substituted cyclohexenyl of formula I connect.
更优选地,所述R1、R2、R3、R4和,R5、R6、R7和R8中的碳链部分分别独立的选自C1~C5的烷基中的一种。More preferably, the carbon chain parts in R1, R2, R3, R4 and R5, R6, R7 and R8 are independently selected from one of C1-C5 alkyl groups.
最优选地,所述R2和R6分别为丙基和亚氨基取代丙基或如式Ⅵ所示分子式,所述R3、R4、R5、R7和R8分别为甲基;Most preferably, the R2 and R6 are respectively propyl and imino substituted propyl or the molecular formula shown in formula VI, and the R3, R4, R5, R7 and R8 are respectively methyl;
Figure PCTCN2021117481-appb-000004
Figure PCTCN2021117481-appb-000004
其中,m3和n3分别选自选自不小于1的整数,具体的如m3为2,n3为3。Wherein, m3 and n3 are respectively selected from integers not less than 1, specifically, m3 is 2, and n3 is 3.
具体的,氨基化聚硅氧烷的制备是基于氨基二烷氧基硅烷偶联剂、二甲基二烷氧基硅烷与六甲基二硅氧烷水解、封端制备而成,氨基接枝率的计算按照核磁法,通过计算氨基峰面积与Si-CH3峰面积的比值进行计算:Specifically, the preparation of aminated polysiloxane is based on aminodialkoxysilane coupling agent, dimethyldialkoxysilane and hexamethyldisiloxane hydrolysis, capping preparation, amino grafting The calculation of the rate is according to the NMR method, by calculating the ratio of the amino peak area to the Si-CH3 peak area:
接枝率=3×氨基峰面积/2×Si-CH3峰面积×100%。Grafting rate=3*amino peak area/2*Si-CH3 peak area*100%.
优选地,所述m1值与m2值之间比值为1:1.5,以保证Diels-Alder反应能够完全进行。Preferably, the ratio between the m1 value and the m2 value is 1:1.5, so as to ensure that the Diels-Alder reaction can proceed completely.
可选地,所述改性聚硅氧烷A和改性聚硅氧烷B分别为线性聚硅氧烷,增加制得的有机硅聚合材料的柔性和成膜性。Optionally, the modified polysiloxane A and the modified polysiloxane B are linear polysiloxanes respectively, which increases the flexibility and film-forming properties of the obtained organosilicon polymer material.
根据本申请的另一个方面,提供了一种自修复的有机硅聚合材料的制备方法,其包括下述步骤:According to another aspect of the present application, a method for preparing a self-healing silicone polymer material is provided, which includes the following steps:
提供改性聚硅氧烷A,所述改性聚硅氧烷A为1分子中具有至少一个马来酰亚胺基取代的聚硅氧烷A;Provide modified polysiloxane A, the modified polysiloxane A is polysiloxane A having at least one maleimide group substitution in one molecule;
提供改性聚硅氧烷B,所述改性聚硅氧烷B为1分子中具有至少一个呋喃乙酰基取代的聚硅氧烷B;Provide modified polysiloxane B, said modified polysiloxane B is polysiloxane B having at least one furoacetyl group substitution in one molecule;
将所述改性聚硅氧烷A和改性聚硅氧烷B溶解后加热使得发生Diels-Alder反应,生成至少一个可逆取代环己烯交联的所述有机硅聚合材料。The modified polysiloxane A and modified polysiloxane B are dissolved and then heated to cause a Diels-Alder reaction to generate the organosilicon polymer material crosslinked by at least one reversibly substituted cyclohexene.
可选地,所述改性聚硅氧烷A的制备方法包括下述步骤:Optionally, the preparation method of the modified polysiloxane A comprises the following steps:
提供氨基化聚硅氧烷A;Aminated polysiloxane A is provided;
将氨基化聚硅氧烷A和马来酸酐溶解在有机溶剂Ⅰ后,加热回流至少3h,即制得所述改性聚硅氧烷A。The modified polysiloxane A is obtained by dissolving the aminated polysiloxane A and maleic anhydride in the organic solvent I and heating to reflux for at least 3 hours.
可选地,所述氨基化聚硅氧烷A的分子量为2000~20000;和所述氨基化聚硅氧烷A中的氨基的接枝率为3%-30%,以氨基计所述氨基化聚硅氧烷A与所述马来酸酐的摩尔比为1:1-3。所述氨基化聚硅氧烷A的重均分子量范围2000-20000,因氨基接枝率较低,该分子量范围可促使分子链在良性溶剂中自由舒展,有利于马来酸酐与侧链中的氨基进行反应,避免因分子量过大导致的分子链因无法自由伸展所导致的反应不完全问题。所述氨基化聚硅氧烷A中的氨基的接枝率有利于具有较大空间体积的马来酰亚胺官能团的接枝,避免因马来酰亚胺基团间的空间位阻所导致的反应不完全。所述氨基与所述马来酸酐的摩尔比有利于马来酸酐与氨基间进行充分反应,避免了反应不完全问题的出现。Optionally, the molecular weight of the aminated polysiloxane A is 2000-20000; and the grafting rate of the amino groups in the aminated polysiloxane A is 3%-30%, and the amino groups in the amino group The molar ratio of polysiloxane A to the maleic anhydride is 1:1-3. The weight-average molecular weight range of the aminated polysiloxane A is 2000-20000. Because the amino grafting rate is low, this molecular weight range can promote the free stretching of the molecular chain in a benign solvent, which is beneficial to the maleic anhydride and the side chain. The amino group reacts to avoid the incomplete reaction caused by the inability of the molecular chain to stretch freely due to too large a molecular weight. The grafting rate of amino groups in the aminated polysiloxane A is conducive to the grafting of maleimide functional groups with larger steric volumes, avoiding the steric hindrance between maleimide groups. The response is incomplete. The molar ratio of the amino group to the maleic anhydride is favorable for the sufficient reaction between the maleic anhydride and the amino group, avoiding the problem of incomplete reaction.
具体的,所述氨基化聚硅氧烷A的重均分子量的范围的上限、下限分别可以选自3000、5000、8000、11000、14000、17000或19000,具体的氨基化聚硅氧烷A的重均分子量可以为3000、5000、8000、10000或15000。Specifically, the upper and lower limits of the weight average molecular weight range of the aminated polysiloxane A can be selected from 3000, 5000, 8000, 11000, 14000, 17000 or 19000, respectively. The weight average molecular weight may be 3000, 5000, 8000, 10000 or 15000.
优选地,所述氨基化聚硅氧烷A中的氨基的接枝率为3%-30%。更进一步地,所述氨基化聚硅氧烷A中的氨基的接枝率为10%-15%。Preferably, the grafting rate of amino groups in the aminated polysiloxane A is 3%-30%. Furthermore, the grafting rate of amino groups in the aminated polysiloxane A is 10%-15%.
优选地,以氨基计所述氨基化聚硅氧烷A与所述马来酸酐的摩尔比为1:1.5-2.5。Preferably, the molar ratio of the aminated polysiloxane A to the maleic anhydride in terms of amino groups is 1:1.5-2.5.
优选地,所述有机溶剂Ⅰ为冰醋酸。Preferably, the organic solvent I is glacial acetic acid.
可选地,将氨基化聚硅氧烷A和马来酸酐溶解在有机溶剂Ⅰ后,加热反应温度为140-180℃,回流反应时间为4-8h,即制得所述改性聚硅氧烷A。Optionally, after dissolving aminated polysiloxane A and maleic anhydride in organic solvent I, the heating reaction temperature is 140-180°C, and the reflux reaction time is 4-8h, that is, the modified polysiloxane Alkane A.
可选地,所述改性聚硅氧烷B的制备方法包括下述步骤:Optionally, the preparation method of the modified polysiloxane B comprises the following steps:
提供氨基化聚硅氧烷B;Aminated polysiloxane B is provided;
在非活性气氛中,将溶于有机溶剂Ⅱ的氨基化聚硅氧烷B和缚酸剂混合后,加入溶于有机溶剂Ⅱ的呋喃乙酰氯,加热回流反应至少0.5h,即制得所述改性聚硅氧烷B。In an inert atmosphere, after mixing the aminated polysiloxane B dissolved in the organic solvent II and the acid-binding agent, adding furoacetyl chloride dissolved in the organic solvent II, and heating under reflux for at least 0.5 hours, the described Modified Polysiloxane B.
优选地,所述氨基化聚硅氧烷B的分子量为2000~20000;Preferably, the molecular weight of the aminated polysiloxane B is 2000-20000;
所述氨基化聚硅氧烷B中的氨基的接枝率为3%-30%,所述氨基与所述呋喃乙酰氯的摩尔比为1:1-5;所述缚酸剂与所述氨基化聚硅氧烷B的质量比为3wt%-7wt%。所述氨基化聚硅氧烷B的重均分子量范围,有利于呋喃乙酰氯与氨基化聚硅氧烷中氨基侧链的反应,避免反应不完全现象出现。所述氨基化聚硅氧烷B中的氨基的接枝率有利于氨基侧链在聚硅氧烷主链上的分散分布,避免因分散过于集中导致的反应不完全问题。所述氨基与所述呋喃乙酰氯的摩尔比有利于呋喃乙酰氯与侧链氨基之间反应的完全性,避免反应不完全。所述缚酸剂与所述氨基化聚硅氧烷B的质量比有利于及时吸附酰氯与氨基反应所产生的氯化氢,避免因酸度过高导致的聚硅氧烷链节的断裂。The grafting rate of the amino group in the aminated polysiloxane B is 3%-30%, and the molar ratio of the amino group to the furoacetyl chloride is 1:1-5; the acid-binding agent and the The mass ratio of aminated polysiloxane B is 3wt%-7wt%. The weight-average molecular weight range of the aminated polysiloxane B is beneficial to the reaction between furoacetyl chloride and the amino side chain in the aminated polysiloxane, and avoids incomplete reaction. The grafting ratio of amino groups in the aminated polysiloxane B is beneficial to the dispersed distribution of amino side chains on the polysiloxane main chain, and avoids the problem of incomplete reaction caused by too concentrated dispersion. The molar ratio of the amino group to the furoyl chloride is conducive to the completeness of the reaction between the furoyl chloride and the side chain amino group, and avoids incomplete reaction. The mass ratio of the acid-binding agent to the aminated polysiloxane B is conducive to the timely adsorption of hydrogen chloride produced by the reaction of acid chlorides and amino groups, and avoids the breakage of polysiloxane chains caused by excessive acidity.
具体的,所述氨基化聚硅氧烷B的重均分子量的范围的上限、下限分别可以选自3000、5000、8000、11000、14000、17000或19000,具体的氨基化聚硅氧烷B的重均分子量可以为3000、5000、8000、10000或15000。Specifically, the upper limit and the lower limit of the range of the weight average molecular weight of the aminated polysiloxane B can be selected from 3000, 5000, 8000, 11000, 14000, 17000 or 19000 respectively, the specific aminated polysiloxane B The weight average molecular weight may be 3000, 5000, 8000, 10000 or 15000.
优选地,所述氨基化聚硅氧烷B中的氨基的接枝率为3%-30%。更进一步地,所述氨基化聚硅氧烷B中的氨基的接枝率为10%-15%。Preferably, the grafting rate of amino groups in the aminated polysiloxane B is 3%-30%. Furthermore, the grafting rate of amino groups in the aminated polysiloxane B is 10%-15%.
优选地,以氨基计所述氨基化聚硅氧烷B与所述呋喃乙酰氯的摩尔比为1:1-1.5。Preferably, the molar ratio of the aminated polysiloxane B to the furoacetyl chloride in terms of amino groups is 1:1-1.5.
优选地,所述缚酸剂与所述氨基化聚硅氧烷B的质量比为4wt%-6wt%。Preferably, the mass ratio of the acid-binding agent to the aminated polysiloxane B is 4wt%-6wt%.
优选地,所述缚酸剂选自吡啶、三乙胺、4-二甲氨基吡啶、碳酸钾、碳酸钠和碳酸铯中的至少一种。更优选地,所述缚酸剂为吡啶类。Preferably, the acid-binding agent is at least one selected from pyridine, triethylamine, 4-dimethylaminopyridine, potassium carbonate, sodium carbonate and cesium carbonate. More preferably, the acid-binding agent is pyridines.
优选地,所述有机溶剂Ⅱ选自无水乙醚、四氢呋喃和二氯甲烷中的至少一种。Preferably, the organic solvent II is at least one selected from anhydrous ether, tetrahydrofuran and dichloromethane.
可选地,在氮气气氛中,将溶于有机溶剂Ⅱ的氨基化聚硅氧烷B和缚酸剂混合后,加入溶于有机溶剂Ⅱ的呋喃乙酰氯,加热回流反应1-3h,即制得所述改性聚硅氧烷B。Alternatively, in a nitrogen atmosphere, after mixing the aminated polysiloxane B dissolved in the organic solvent II and the acid-binding agent, add furoacetyl chloride dissolved in the organic solvent II, and heat and reflux for 1-3 hours to obtain The modified polysiloxane B was obtained.
可选地,所述改性聚硅氧烷A和改性聚硅氧烷B溶于有机溶剂Ⅲ后在150℃-200℃的温度下反应至少15h,优选24h-48h,以保证反应产率可达95%以上。Optionally, the modified polysiloxane A and modified polysiloxane B are dissolved in the organic solvent III and reacted at a temperature of 150°C-200°C for at least 15h, preferably 24h-48h, to ensure the reaction yield It can reach more than 95%.
以马来酰亚胺基计的改性聚硅氧烷A和以呋喃乙酰基的改性聚硅氧烷B的摩尔比为1:1-4。优选地,以马来酰亚胺基计的改性聚硅氧烷A和以呋喃乙酰基的改性聚硅氧烷B的摩尔比为1:2-3。The molar ratio of modified polysiloxane A based on maleimide group to modified polysiloxane B based on furoacetyl group is 1:1-4. Preferably, the molar ratio of the modified polysiloxane A based on maleimide groups to the modified polysiloxane B based on furoacetyl groups is 1:2-3.
优选地,所述有机溶剂Ⅲ选自二甲醚、二甲苯、苯甲醇、二甲酸酯和苯甲酸乙酯中的一种。Preferably, the organic solvent III is selected from one of dimethyl ether, xylene, benzyl alcohol, dicarboxylate and ethyl benzoate.
根据本申请的另一方面,提供了一种上述任一项所述的缓释包膜肥料的制备方法,其包括下述步骤:According to another aspect of the present application, there is provided a method for preparing the slow-release coated fertilizer described in any one of the above, which includes the following steps:
提供具有目标目数的所述肥料颗粒;providing said fertilizer granules having a target mesh;
提供所述有机硅聚合材料;providing said silicone polymeric material;
将所述肥料颗粒加入转鼓包衣机中,调整包衣机以35°-45°角度旋转,预热控制肥料颗粒表面微熔;Add the fertilizer granules into the drum coating machine, adjust the coating machine to rotate at an angle of 35°-45°, and preheat to control the micro-melting of the surface of the fertilizer granules;
将溶于有机溶剂Ⅵ的所述有机硅聚合材料喷到所述肥料颗粒的表面,即制得所述的缓释包膜肥料。Spray the organosilicon polymer material dissolved in the organic solvent VI onto the surface of the fertilizer granules to obtain the slow-release coated fertilizer.
本申请中通过控制包衣机的角度进一步控制包衣机中的肥料颗粒呈现连续式料帘,从而能够使得有机硅聚合材料能够直接喷在悬空的肥料颗粒的表面并成膜后再落入包衣机内腔壁上,更有利于包膜成膜的均匀性。另外,控制温度使得肥料的表面出现微熔有利于肥料表面与有机硅聚合材料更好的粘连结合在一起。In this application, by controlling the angle of the coating machine, the fertilizer particles in the coating machine are further controlled to present a continuous material curtain, so that the organosilicon polymer material can be directly sprayed on the surface of the suspended fertilizer particles and form a film before falling into the coating. On the inner wall of the clothing machine, it is more conducive to the uniformity of film formation. In addition, controlling the temperature to make the surface of the fertilizer micro-melt is conducive to better adhesion and bonding of the fertilizer surface and the organic silicon polymer material.
可选地,所述包衣机旋转的速度为40-80r/m。优选地,所述包衣机旋转的速度为50-70r/m。该旋转速度的控制可以防止包膜肥料出现相互粘结的情况。Optionally, the coating machine rotates at a speed of 40-80r/m. Preferably, the rotating speed of the coating machine is 50-70r/m. The control of the rotation speed can prevent the coated fertilizers from sticking to each other.
可选地,所述有机硅聚合材料与所述肥料颗粒的质量比为1%-8%。Optionally, the mass ratio of the organosilicon polymer material to the fertilizer granules is 1%-8%.
可选地,所述预热肥料颗粒的温度为80-140℃。优选地,所述预热肥料颗粒的温度为90-110℃。所述的预热温度优选适用的肥料为尿素。Optionally, the temperature of the preheated fertilizer granules is 80-140°C. Preferably, the temperature of the preheated fertilizer granules is 90-110°C. The fertilizer preferably applicable to the preheating temperature is urea.
本申请的有益效果包括但不限于:The beneficial effects of this application include but are not limited to:
1.根据本申请的缓释包膜肥料,缓释包膜肥料中包膜使用的包膜有机硅聚合材料可在特定的温度下实现交联键的断裂和交联,在作为肥料包膜材料,利用Diels-Alder反应具有温度可逆性,可通过温度控制化学键的键合和解离特点,若出现包膜不均时,可重复进行多次包膜处理,减少了残次率,提高了包膜成品率,并且避免了包膜不均所引起的肥料缓释效果不佳的问题。1. According to the slow-release coated fertilizer of the present application, the coated organosilicon polymer material used in the slow-release coated fertilizer can realize the breaking and cross-linking of cross-linked bonds at a specific temperature, and can be used as a fertilizer coating material , using the temperature reversibility of the Diels-Alder reaction, the bonding and dissociation characteristics of chemical bonds can be controlled by temperature. If the coating is uneven, the coating treatment can be repeated many times, reducing the defective rate and improving the coating quality. The yield rate is high, and the problem of poor fertilizer slow-release effect caused by uneven coating is avoided.
2.根据本申请的缓释包膜肥料,缓释包膜肥料中包膜有机硅材料具有的Si-O链段虽具有极强的疏水特性,但马来酰亚胺基团和呋喃乙酰化基团的可逆交联为复合材料内部提供了孔洞,保证了包膜肥料的缓释效果。2. According to the slow-release coated fertilizer of the present application, although the Si-O segment of the coated organic silicon material in the slow-release coated fertilizer has extremely strong hydrophobic properties, the maleimide group and furan acetylation The reversible cross-linking of the group provides holes inside the composite material, which ensures the slow-release effect of the coated fertilizer.
3.根据本申请的缓释包膜肥料,缓释包膜肥料能够实现产业化,具有巨大的经济价值和行业影响力;具有绿色环保,可以实现“高分子材料的资源化”,具有巨大的开发潜力。3. According to the slow-release coated fertilizer of the present application, the slow-release coated fertilizer can realize industrialization and has huge economic value and industry influence; it is green and environmentally friendly, and can realize "recycling of polymer materials" and has huge potential develop potential.
4.根据本申请的缓释包膜肥料的制备方法,其包膜形成的薄膜均匀,肥料颗粒与薄膜结合性好,可以重复加工以修复产生的包膜不均匀问题,以避免解决因包膜不均匀而产生废料。4. According to the preparation method of the slow-release coated fertilizer of the present application, the film formed by the coating is uniform, the fertilizer particles and the film are well bonded, and the process can be repeated to repair the uneven coating produced, so as to avoid solving the problem caused by the coating. Non-uniformity produces waste.
5.根据本申请的缓释包膜肥料的制备方法,缓释包膜肥料中使用的包膜有机硅聚合材料其是马来酰亚胺功能化和呋喃乙酰化聚硅氧烷之间利用无催化剂型Diels-Alder反应所构建,不存在催化剂去除及残留问题,后处理步骤简便。5. According to the preparation method of the slow-release coated fertilizer of the present application, the coated organosilicon polymer material used in the slow-release coated fertilizer is a mixture of maleimide functionalization and furan acetylated polysiloxane. Constructed by catalyst-type Diels-Alder reaction, there is no problem of catalyst removal and residue, and the post-treatment steps are simple.
附图说明Description of drawings
此处所说明的附图用来提供对本申请的进一步理解,构成本申请的一部分,本申请的示意性实施例及其说明用于解释本申请,并不构成对本申请的不当限定。在附图中:The drawings described here are used to provide a further understanding of the application and constitute a part of the application. The schematic embodiments and descriptions of the application are used to explain the application and do not constitute an improper limitation to the application. In the attached picture:
图1(A)和(B)分别为本申请实施例1涉及的马来酰亚胺化聚硅氧烷A1#、呋喃乙酰化聚硅氧烷B1#红外谱图;Fig. 1 (A) and (B) are respectively the infrared spectrograms of maleimidated polysiloxane A1# and furan acetylated polysiloxane B1# involved in Example 1 of the present application;
图2(A)和(B)分别为实施例1及的马来酰亚胺化聚硅氧烷A1#、呋喃乙酰化聚硅氧烷B1#GPC谱图;Fig. 2 (A) and (B) are respectively embodiment 1 and maleimidated polysiloxane A1#, furan acetylated polysiloxane B1# GPC spectrogram;
图3(A)为有机硅聚合材料1#在氮气和空气下的热重分析图;(B)为有机硅聚合材料1#的DSC谱图;Fig. 3 (A) is the thermogravimetric analysis figure of organosilicon polymer material 1# under nitrogen and air; (B) is the DSC spectrogram of organosilicon polymer material 1#;
图4为实施例1所得到的有机硅聚合材料1#的微观结构示意图;Fig. 4 is the microstructure schematic diagram of the organosilicon polymer material 1# obtained in embodiment 1;
图5为实施例1所得到的有机硅聚合材料1#的光学性能谱图,(A)为紫外光谱和(B)为荧光谱图;Fig. 5 is the optical performance spectrogram of the organosilicon polymer material 1# obtained in embodiment 1, (A) is the ultraviolet spectrum and (B) is the fluorescence spectrogram;
图6(A)为实施例2使用的尿素原颗粒图;(B)为有机硅聚合材料1# 包膜尿素颗粒后的包膜肥料1#照片;Fig. 6 (A) is the urea granule figure that embodiment 2 uses; (B) is the coated fertilizer 1# photograph behind the organosilicon polymeric material 1# coated urea granule;
图7为60d内实施例2、4、6分别制得的包膜肥料1#-3#缓释特性谱图;Fig. 7 is the coated fertilizer 1#-3# slow-release property spectrogram that embodiment 2,4,6 makes respectively in 60d;
图8为实施例2所得到的有机硅复合肥料自修复图,(A)尿素释放后的有机硅聚合材料1#壳;(B)发生Diels-Alder逆反应修复后的有机硅聚合材料2#壳。Fig. 8 is the self-repair diagram of the organosilicon compound fertilizer obtained in Example 2, (A) the 1# shell of the organosilicon polymer material after urea release; (B) the 2# shell of the organosilicon polymer material after the Diels-Alder reverse reaction repair occurred .
图9为实施例中的制备有机硅聚合材料过程和结构示意图。Fig. 9 is a schematic diagram of the process and structure of the preparation of the organosilicon polymer material in the embodiment.
具体实施方式Detailed ways
下面结合实施例详述本申请,但本申请并不局限于这些实施例。The present application is described in detail below in conjunction with the examples, but the present application is not limited to these examples.
“烃基”是包括烷基、烯基、炔基和芳基。"Hydrocarbyl" includes alkyl, alkenyl, alkynyl and aryl.
“烷基”是指单价脂族烃基。烷基可具有任何数量的碳原子。许多烷基基团为C1至C30。一些烷基可为C1或更大,诸如C2或更大,C4或更大,C6或更大,或者C8或更大。一些烷基可为C22或更小,C16或更小,C12或更小,C8或更小,或者C4或更小。除非另外指明,否则任何烷基可独立地为直链的、支链的、环状的、或它们的组合(例如,环状烷基也可具有直链或支链的组分。)示例性烷基包括甲基、乙基、丙基、异丙基、正丁基、叔丁基、仲丁基、异丁基、2-乙基己基、异辛基、十二烷基、十六烷基、二十二烷基等等。"Alkyl" means a monovalent aliphatic hydrocarbon group. An alkyl group can have any number of carbon atoms. Many alkyl groups are C1 to C30. Some alkyl groups can be C1 or larger, such as C2 or larger, C4 or larger, C6 or larger, or C8 or larger. Some alkyl groups can be C22 or less, C16 or less, C12 or less, C8 or less, or C4 or less. Unless otherwise specified, any alkyl groups may independently be linear, branched, cyclic, or combinations thereof (eg, cyclic alkyl groups may also have linear or branched components.) Exemplary Alkyl includes methyl, ethyl, propyl, isopropyl, n-butyl, tert-butyl, sec-butyl, isobutyl, 2-ethylhexyl, isooctyl, dodecyl, hexadecane base, docosyl group and so on.
“芳基”是指单价芳族基团。芳基可包括仅碳和氢,或者也可包括一个或多个杂原子,诸如氧、氮和硫中的一种或多种。芳基可具有带三个或更多个原子、四个或更多个原子、或者五个或更多个原子的芳族环。芳基可具有带十个或更少个原子、八个或更少个原子、七个或更少个原子、或者六个或更少个原子的环。示例性芳基包括苯基、呋喃基、萘基、蒽基等等。苯基是常见的芳基取代基。"Aryl" refers to a monovalent aromatic group. Aryl groups may include only carbon and hydrogen, or may also include one or more heteroatoms, such as one or more of oxygen, nitrogen, and sulfur. Aryl groups can have an aromatic ring with three or more atoms, four or more atoms, or five or more atoms. Aryl groups can have rings with ten or fewer atoms, eight or fewer atoms, seven or fewer atoms, or six or fewer atoms. Exemplary aryl groups include phenyl, furyl, naphthyl, anthracenyl, and the like. Phenyl is a common aryl substituent.
“氨基”是指具有式-Nc(H)p(R′)q的基团,其中每个R′独立地为烷基、烯基、炔基、芳基或烷芳基,它们中的任一个可为任选地取代的,p+q为2或3,并且c代表氮原子上的电荷,其为0或1+。通常,每个R′为烷基。当p+q为2时,c为0;当p+q为3时,c为1+。氨基基团可为伯氨、仲氨、叔氨或季氨,具体取决于q的值。q值为0、1、2和3的氨基基团分别为伯氨、仲氨、叔氨和季氨。"Amino" means a group having the formula -Nc(H)p(R')q, wherein each R' is independently an alkyl, alkenyl, alkynyl, aryl, or alkaryl group, any of which One may be optionally substituted, p+q is 2 or 3, and c represents the charge on the nitrogen atom, which is 0 or 1+. Typically, each R' is an alkyl group. When p+q is 2, c is 0; when p+q is 3, c is 1+. The amino group can be primary, secondary, tertiary or quaternary, depending on the value of q. Amino groups with q values of 0, 1, 2 and 3 are primary, secondary, tertiary and quaternary ammonia, respectively.
“聚二有机硅氧烷”是指具有重复单元-Si(G) 2O-的聚合物,其中每次出现的G独立地为有机部分。每次出现的G通常独立地为烷基、芳基、烯基或炔基。烷基和芳基是最常见的,并且烷基比芳基更常见。当G为芳基时,其可为任何芳基基团,例如在本文中以“芳基”的定义所涉及的任何基团。典型的芳基基团包括苯基。典型的烷基基团包括参考本文中烷基的定义所讨论的那些,并且也包括C1至C22烷基、C1至C16烷基、C1至C12烷基、C1至C8烷基、或C1至C4烷基,诸如甲基、乙基、丙基、丁基(诸如叔丁基、异丁基、正丁基和仲丁基)、和C8烷基,诸如2-乙基己基和异辛基。当未指 定时,聚二有机硅氧烷的端基可改变;典型的端基包括三有机甲硅烷基基团和羟基基团,以及封端基团、淬灭基团和链转移基团。 "Polydiorganosiloxane" refers to a polymer having the repeating unit -Si(G) 2O- , wherein each occurrence of G is independently an organic moiety. Each occurrence of G is typically independently alkyl, aryl, alkenyl or alkynyl. Alkyl and aryl are the most common, and alkyl is more common than aryl. When G is aryl, it may be any aryl group, for example any group referred to herein by the definition of "aryl". Typical aryl groups include phenyl. Typical alkyl groups include those discussed with reference to the definition of alkyl herein, and also include C1 to C22 alkyl, C1 to C16 alkyl, C1 to C12 alkyl, C1 to C8 alkyl, or C1 to C4 Alkyl groups such as methyl, ethyl, propyl, butyl (such as tert-butyl, isobutyl, n-butyl and sec-butyl), and C8 alkyl groups such as 2-ethylhexyl and isooctyl. When not specified, the end groups of polydiorganosiloxanes can vary; typical end groups include triorganosilyl groups and hydroxyl groups, as well as capping, quenching, and chain transfer groups .
如无特别说明,本申请的实施例中的原料、试剂和肥料通过商业途径购买。其中,原料氨基化聚硅氧烷为实验室自制,利用氨丙基甲基二乙氧基硅烷或3-(2-氨乙基)-氨丙基甲基二乙氧基硅烷与二甲基二乙氧基硅烷水解制备而成侧氨基聚硅氧烷,氨丙基二甲基乙氧基硅烷或3-(2-氨乙基)-氨丙基二甲基乙氧基硅烷水解制备而成。Unless otherwise specified, the raw materials, reagents and fertilizers in the examples of the present application were purchased through commercial channels. Among them, the raw material aminated polysiloxane is self-made in the laboratory, using aminopropylmethyldiethoxysilane or 3-(2-aminoethyl)-aminopropylmethyldiethoxysilane and dimethyl Side aminopolysiloxane prepared by hydrolysis of diethoxysilane, prepared by hydrolysis of aminopropyldimethylethoxysilane or 3-(2-aminoethyl)-aminopropyldimethylethoxysilane become.
本申请的实施例中分析方法如下:Analytic method is as follows in the embodiment of the application:
利用美国尼高力公司Nicolet710型号红外仪器进行红外分析测试;Use the Nicolet710 infrared instrument of Nicolet Company of the United States to conduct infrared analysis and testing;
利用美国怀雅特公司DAWN HELEOS II型号凝胶渗透色谱仪器进行凝胶渗透色谱(GPC)分析测试;Gel Permeation Chromatography (GPC) analysis test was carried out by using DAWN HELEOS II Gel Permeation Chromatography Instrument of Wyatt Company of the United States;
利用梅特勒-托利公司TGA2热分析仪器进行热分析测试;Use Mettler-Tolley TGA2 thermal analysis instrument for thermal analysis test;
利用德国蔡司公司SUPRA
Figure PCTCN2021117481-appb-000005
55型号扫描电子显微镜进行微观结构分析测试;
Using German Zeiss company SUPRA
Figure PCTCN2021117481-appb-000005
Model 55 scanning electron microscope for microstructure analysis and testing;
利用Agilent公司Cary 5000型号仪器进行紫外光谱测试;Utilize the Cary 5000 model instrument of Agilent Company to carry out the ultraviolet spectrum test;
利用爱丁堡公司FLS-1000型号仪器进行荧光光谱分析测试;Use the FLS-1000 model instrument of Edinburgh company to carry out the fluorescence spectrum analysis test;
利用GB/T23348-2009中的复混肥料中总氮含量测定-蒸馏后滴定法进行水中氮素释放率的分析测试;测试方法为水中浸泡的方法,用水或一定浓度的盐溶液浸提包膜控释肥,以计算一定时间内养分的溶出量。将4g待测肥料加入盛有80mL去离子水的烧杯中,并在上面加盖,置于30℃恒温箱中培养,每隔6h取样1次,每次取2.5mL,测定浸出液中的氮含量。Using GB/T23348-2009 Determination of Total Nitrogen Content in Compound Fertilizers-Distillation Titration Method to analyze and test the release rate of nitrogen in water; the test method is the method of soaking in water, leaching the coating with water or a certain concentration of salt solution Controlled-release fertilizers to calculate the amount of nutrients dissolved within a certain period of time. Add 4g of the fertilizer to be tested into a beaker filled with 80mL of deionized water, cover it, place it in a 30°C incubator, and take samples every 6h, taking 2.5mL each time to measure the nitrogen content in the leachate .
参考图9,图中示意可逆反应和热自修复的过程,和制得的有机硅复合材料结构示意图,其中,1为聚硅氧烷中的Si-O-Si链段,2为马来酰亚胺基,3为呋喃乙酰基,4为
Figure PCTCN2021117481-appb-000006
Referring to Figure 9, the figure shows the process of reversible reaction and thermal self-repair, and the structure diagram of the obtained organosilicon composite material, in which, 1 is the Si-O-Si segment in polysiloxane, and 2 is maleyl Imino group, 3 is furoacetyl, 4 is
Figure PCTCN2021117481-appb-000006
出反应的过程和根据本申请的一种实施方式,自修复有机硅聚合材料的制备方法,包括下述步骤:The process of reacting and according to an embodiment of the present application, the preparation method of self-healing silicone polymer material comprises the following steps:
步骤一、改性聚硅氧烷A(马来酰亚胺化聚硅氧烷A)制备:将分散于30mL冰醋酸中的具有不同分子量、不同氨基含量的端氨基化聚硅氧烷A或侧氨基化聚硅氧烷A和马来酸酐置于装有导气管,恒压低液漏斗和球形冷凝管的100mL圆底烧瓶中,在电磁搅拌下加热至140-180℃并回流反应4-8h后,减压除去冰醋酸并用氯仿溶解残留物,饱和氯化钠水溶液纯化洗涤数次后将有机相分离;有机相中加入无水硫酸镁干燥过夜后,减压除去有机溶剂得到棕色透明油状液体,即制得改性聚硅氧烷A; Step 1, preparation of modified polysiloxane A (maleimidated polysiloxane A): Amine-terminated polysiloxane A or Side aminated polysiloxane A and maleic anhydride were placed in a 100mL round-bottomed flask equipped with an air duct, a constant pressure low liquid funnel and a spherical condenser, heated to 140-180°C under electromagnetic stirring and refluxed to react 4- After 8 hours, remove glacial acetic acid under reduced pressure and dissolve the residue with chloroform, purify and wash with saturated sodium chloride aqueous solution several times and separate the organic phase; add anhydrous magnesium sulfate to the organic phase and dry overnight, remove the organic solvent under reduced pressure to obtain a brown transparent oil Liquid, that is, the modified polysiloxane A is obtained;
其中,氨基化聚硅氧烷A重均分子量包括但不局限于3000、5000、10000、 15000,氨基化聚硅氧烷A中氨基接枝率包括但不局限于3%-30%,氨基与马来酸酐摩尔比为1:1-1:3;Among them, the weight average molecular weight of aminated polysiloxane A includes but not limited to 3000, 5000, 10000, 15000, the grafting ratio of amino groups in aminated polysiloxane A includes but not limited to 3%-30%. The molar ratio of maleic anhydride is 1:1-1:3;
步骤二、改性聚硅氧烷B(呋喃乙酰化聚硅氧烷B)制备:对50mL圆底烧瓶进行三抽三放后通入氮气进行保护,将具有不同重均分子量、不同氨基含量的端基氨基改性聚硅氧烷B或侧基氨基改性聚硅氧烷B,溶于20mL有机溶剂Ⅱ中,并引入缚酸剂,缚酸剂添加量为氨基改性聚硅氧烷B质量的3%-7%;在电磁搅拌15-30min后,将溶于有机溶剂Ⅱ中的呋喃乙酰氯缓慢滴入圆底烧瓶中,氨基与呋喃乙酰氯摩尔比为1:1-1:1.5,在回流状态下反应1h-3h;抽滤去除产生的盐后进行减压蒸馏纯化,获得浅黄色油状液体,即制得改性聚硅氧烷B; Step 2. Preparation of modified polysiloxane B (furan acetylated polysiloxane B): Three extractions and three discharges were performed on a 50mL round bottom flask, and then nitrogen was introduced for protection. Terminal amino-modified polysiloxane B or pendant amino-modified polysiloxane B, dissolved in 20mL organic solvent II, and introduced acid-binding agent, the amount of acid-binding agent added is amino-modified polysiloxane B 3%-7% of the mass; after electromagnetic stirring for 15-30min, slowly drop the furoyl chloride dissolved in the organic solvent II into the round bottom flask, the molar ratio of amino group to furoyl chloride is 1:1-1:1.5 , and reacted for 1h-3h under reflux; vacuum distillation and purification were performed to remove the generated salt by suction filtration to obtain a light yellow oily liquid, which was to obtain modified polysiloxane B;
其中,氨基改性聚硅氧烷B重均分子量包括但不局限于3000、5000、10000、15000,氨基改性聚硅氧烷B氨基接枝率包括但不局限于3%-30%,有机溶剂Ⅱ包括但不局限于无水乙醚、四氢呋喃、二氯甲烷;缚酸剂包括但不局限于吡啶、三乙胺、4-二甲氨基吡啶、碳酸钾、碳酸钠、碳酸铯等;有机溶剂Ⅱ中的呋喃乙酰氯体积:体积(v:v)比为1:5-1:1 0;Among them, the weight-average molecular weight of amino-modified polysiloxane B includes but is not limited to 3000, 5000, 10000, and 15000, and the amino graft ratio of amino-modified polysiloxane B includes but is not limited to 3%-30%. Solvent II includes but not limited to anhydrous ether, tetrahydrofuran, dichloromethane; acid-binding agents include but not limited to pyridine, triethylamine, 4-dimethylaminopyridine, potassium carbonate, sodium carbonate, cesium carbonate, etc.; organic solvents The volume of furoacetyl chloride in II: the volume (v:v) ratio is 1:5-1:10;
步骤三、有机硅聚合材料制备:将改性聚硅氧烷A(马来酰亚胺化聚硅氧烷A)及改性聚硅氧烷B(呋喃乙酰化聚硅氧烷B)溶于有机溶剂Ⅲ后,转入圆底烧瓶中,在电磁搅拌下加热至150℃-200℃并反应24h-48h;反应完成后倒入无水甲醇溶液中,得到浅红色沉淀,抽滤去除有机溶剂Ⅲ后反复用无水甲醇洗涤数次,真空干燥过夜,即制得有机硅聚合材料; Step 3, preparation of silicone polymer material: Dissolve modified polysiloxane A (maleimidated polysiloxane A) and modified polysiloxane B (furan acetylated polysiloxane B) in After the organic solvent III, transfer to a round bottom flask, heat to 150°C-200°C under electromagnetic stirring and react for 24h-48h; after the reaction is completed, pour it into anhydrous methanol solution to obtain a light red precipitate, remove the organic solvent by suction filtration After Ⅲ, repeatedly wash with anhydrous methanol for several times, and vacuum dry overnight to obtain the organosilicon polymer material;
其中,马来酰亚胺基与呋喃乙酰基的摩尔比为1:1-1:4,有机溶剂Ⅲ包括但不局限于二甲醚、二甲苯、苯甲醇、二甲酸酯、苯甲酸乙酯等。Wherein, the molar ratio of maleimide group to furanacetyl group is 1:1-1:4, organic solvent III includes but not limited to dimethyl ether, xylene, benzyl alcohol, diformic acid ester, ethyl benzoate Esters etc.
根据本申请的另一种实施方式,自修复有机硅聚合材料作为肥料包膜中的应用,包括下述步骤:According to another embodiment of the present application, the application of the self-healing organosilicon polymer material as a fertilizer coating includes the following steps:
有机硅聚合材料作为肥料包膜工艺:将肥料用不同目数(10-40目)的筛子筛分后,分别以50g为一份进行分装;Organosilicon polymer material as fertilizer coating process: After sieving the fertilizer with sieves of different meshes (10-40 mesh), divide the fertilizer into 50g portions;
取一份肥料于转鼓包衣机中,调整包衣机角度为35°-45°,转速控制在40-80r/m,使肥料在包衣机中可以形成连续式料帘;15min后进行预加热,温度控制在约90℃-110℃,使肥料颗粒表面呈现微熔状态,喷入溶于二氯甲烷溶液的有机硅聚合材料,喷入的有机硅聚合材料占肥料质量的0.5%-5%,使其在肥料颗粒表面形成均匀的薄膜。可在紫外灯下观察有机硅聚合材料在肥料颗粒表面包裹的均匀性。进一步地,包膜过程中通过调节转速防止出现相互粘结情况。Take a portion of fertilizer in the rotary drum coater, adjust the angle of the coater to 35°-45°, and control the speed at 40-80r/m, so that the fertilizer can form a continuous material curtain in the coater; carry out pre-treatment after 15 minutes. Heating, the temperature is controlled at about 90°C-110°C, so that the surface of the fertilizer granules is in a slightly molten state, and the organic silicon polymer material dissolved in the methylene chloride solution is sprayed. The injected organic silicon polymer material accounts for 0.5%-5% of the fertilizer mass. %, so that it forms a uniform film on the surface of fertilizer granules. The uniformity of silicone polymer material coating on the surface of fertilizer particles can be observed under ultraviolet light. Further, during the coating process, the rotation speed is adjusted to prevent mutual sticking.
实施例1 有机硅聚合材料1#的制备Example 1 Preparation of organosilicon polymer material 1#
本实施例的改性聚硅氧烷A1#、改性聚硅氧烷B1#反应方程式分别如下所示The reaction equations of modified polysiloxane A1# and modified polysiloxane B1# of the present embodiment are as follows respectively
Figure PCTCN2021117481-appb-000007
Figure PCTCN2021117481-appb-000007
自修复的有机硅聚合材料1#的制备方法包括下述步骤:The preparation method of self-healing organosilicon polymer material 1# comprises the following steps:
(1)改性聚硅氧烷A1#(马来酰亚胺化聚硅氧烷A1#)制备:将分散于30mL冰醋酸中的重均分子量为5000的端氨丙基改性聚硅氧烷和马来酸酐以氨基与马来酸酐摩尔比为1:1的量置于装有导气管,恒压低液漏斗和球形冷凝管的100mL圆底烧瓶中,在电磁搅拌下加热至140℃并回流反应4h后,减压除去冰醋酸并用氯仿溶解残留物,饱和氯化钠水溶液纯化洗涤数次后将有机相分离。有机相中加入无水硫酸镁干燥过夜后,减压除去有机溶剂得到棕色透明油状液体,即制得改性聚硅氧烷A1#(马来酰亚胺化聚硅氧烷A1#),红外测试结果见图1(A),GPC测试GPC谱图见图2(A);(1) Preparation of modified polysiloxane A1# (maleimidated polysiloxane A1#): Aminopropyl-terminated polysiloxane with a weight-average molecular weight of 5000 dispersed in 30 mL of glacial acetic acid Alkanes and maleic anhydride are placed in a 100mL round-bottomed flask equipped with an airway tube, a constant pressure low liquid funnel and a spherical condenser at a molar ratio of amino to maleic anhydride of 1:1, and heated to 140°C under electromagnetic stirring After reflux for 4 hours, the glacial acetic acid was removed under reduced pressure and the residue was dissolved in chloroform, purified and washed several times with saturated aqueous sodium chloride solution, and the organic phase was separated. After adding anhydrous magnesium sulfate to the organic phase and drying it overnight, remove the organic solvent under reduced pressure to obtain a brown transparent oily liquid, that is, the modified polysiloxane A1# (maleimidated polysiloxane A1#), infrared The test results are shown in Figure 1 (A), and the GPC spectrum of the GPC test is shown in Figure 2 (A);
(2)改性聚硅氧烷B1#(呋喃乙酰化聚硅氧烷B1#):对50mL圆底烧瓶进行三抽三放后通入氮气进行保护,为保证改性聚硅氧烷A与改性聚硅氧烷B之间的Diels-Alder反应更完全,所得到的膜的性能更好,所选择的端氨丙基聚硅氧烷与A1#中选择的相同。将重均分子量为5000的端氨丙基改性聚硅氧烷溶于20mL无水乙醚中,加入缚酸剂吡啶,吡啶添加量为端氨丙基改性聚硅氧烷质量的3%;在电磁搅拌15min后,将以体积质量比(mL:g)为10:1的溶于有机溶剂无水乙醚中的呋喃乙酰氯缓慢滴入圆底烧瓶中,其中氨基与呋喃乙酰氯摩尔比为1:1,在回流状态下反应1h后,抽滤去除产生的盐后进行减压蒸馏纯化,获得浅黄色油状液体,即制得改性聚硅氧烷B1#,红外测试结果见图1(B),GPC测试GPC谱图见图2(B);(2) Modified polysiloxane B1# (furan acetylated polysiloxane B1#): the 50mL round-bottomed flask was pumped three times and vented three times, and then passed into nitrogen for protection. In order to ensure the modified polysiloxane A and The Diels-Alder reaction between the modified polysiloxane B is more complete, and the performance of the obtained film is better, and the selected aminopropyl polysiloxane is the same as that selected in A1#. Dissolve aminopropyl-terminated polysiloxane with a weight-average molecular weight of 5000 in 20 mL of anhydrous ether, add acid-binding agent pyridine, and the amount of pyridine added is 3% of the mass of aminopropyl-terminated polysiloxane; After electromagnetic stirring for 15 min, furoyl chloride dissolved in the organic solvent anhydrous ether with a volume to mass ratio (mL:g) of 10:1 was slowly dropped into the round-bottomed flask, wherein the molar ratio of amino group to furoyl chloride was 1:1, after reacting for 1 hour under reflux, remove the generated salt by suction filtration, and carry out vacuum distillation and purification to obtain a light yellow oily liquid, which is the modified polysiloxane B1#. The infrared test results are shown in Figure 1 ( B), GPC test GPC spectrogram is shown in Fig. 2 (B);
(3)有机硅聚合材料1#制备:将马来酰亚胺化聚硅氧烷A1#及呋喃乙酰化聚硅氧烷B1#分别以马来酰亚胺基与呋喃乙酰基计摩尔比为1:2溶于有机溶剂二甲醚中,溶剂与原料之间的体积质量比(mL:g)为20:1,并转入圆底烧瓶中,在电磁搅拌下加热至150℃并反应24h后倒入无水甲醇溶液中,得到浅红色沉淀,抽滤去除溶剂后反复用无水甲醇洗涤数次,真空干燥过夜得有机硅聚合材料1#。(3) Preparation of organosilicon polymer material 1#: Maleimidated polysiloxane A1# and furanacetylated polysiloxane B1# were calculated by maleimide group and furanacetyl group in a molar ratio of 1:2 dissolved in the organic solvent dimethyl ether, the volume-to-mass ratio (mL:g) between the solvent and the raw material is 20:1, and transferred to a round bottom flask, heated to 150°C under electromagnetic stirring and reacted for 24h Then pour it into anhydrous methanol solution to obtain a light red precipitate, remove the solvent by suction filtration, wash with anhydrous methanol several times, and dry in vacuo overnight to obtain organosilicon polymer material 1#.
有机硅聚合材料1#在氮气和空气下的热重分析见图3(A),机硅聚合材料1#DSC谱图见图3(B),有机硅聚合材料1#微观结构示意图见图4。有机硅复合材料1#的紫外光谱见图5(A)和荧光谱图见图5(B)。The thermogravimetric analysis of organosilicon polymer material 1# under nitrogen and air is shown in Figure 3(A), the DSC spectrum of organosilicon polymer material 1# is shown in Figure 3(B), and the schematic diagram of the microstructure of organosilicon polymer material 1# is shown in Figure 4 . The ultraviolet spectrum of organosilicon composite material 1# is shown in Figure 5(A) and the fluorescence spectrum is shown in Figure 5(B).
实施例2 包膜肥料1#的制备The preparation of embodiment 2 coated fertilizer 1#
使用实施例1#的有机硅聚合材料1#作为肥料包膜工艺:将尿素用10目的筛子筛分后,分别以50g为一份进行分装;取一份尿素于转鼓包衣机中,调整包衣机角度为35°,转速控制在40r/m,使尿素在包衣机中可以形成连续式料帘;15min后进行预加热,温度控制在约90℃,使尿素颗粒表面呈现微熔状态,喷入溶于二氯甲烷溶液的有机硅聚合材料1#,有机硅聚合材料1#添加量选取肥料质量的1%,包膜过程中通过调节转速防止出现相互粘结情况,使有机硅聚合材料1#在尿素颗粒表面形成均匀的薄膜,制得包膜肥料1#。Use the organosilicon polymeric material 1# of embodiment 1# as the fertilizer coating process: after sieving the urea with a 10-mesh sieve, pack it with 50g as a portion; get a portion of urea in a drum coating machine, adjust The angle of the coating machine is 35°, and the speed is controlled at 40r/m, so that the urea can form a continuous material curtain in the coating machine; preheat after 15 minutes, and the temperature is controlled at about 90°C, so that the surface of the urea particles is in a slightly molten state , spray into the organosilicon polymer material 1# dissolved in dichloromethane solution, the addition amount of the organosilicon polymer material 1# is selected as 1% of the fertilizer mass, and the rotation speed is adjusted during the coating process to prevent mutual adhesion, so that the organosilicon polymerizes Material 1# forms a uniform film on the surface of urea granules to obtain coated fertilizer 1#.
通过紫外灯下观察有机硅聚合材料在尿素颗粒表面包裹的均匀性。图6(A)为尿素原颗粒照片;图6(B)为包膜肥料1#的照片。Observe the uniformity of silicone polymer material wrapping on the surface of urea particles under ultraviolet light. Fig. 6(A) is a photo of urea granules; Fig. 6(B) is a photo of coated fertilizer 1#.
实施例3 有机硅聚合材料2#的制备Example 3 Preparation of organosilicon polymer material 2#
自修复的有机硅聚合材料2#的制备方法包括下述步骤:The preparation method of self-repairing organosilicon polymer material 2# comprises the following steps:
(1)改性聚硅氧烷A2#(马来酰亚胺化聚硅氧烷A2#)制备:将分散于30mL冰醋酸中的重均分子量为5000的侧氨丙基改性聚硅氧烷和马来酸酐以氨基与马来酸酐摩尔比为1:3的量置于装有导气管,氨基接枝率15%,恒压低液漏斗和球形冷凝管的100mL圆底烧瓶中,在电磁搅拌下加热至160℃并回流反应6h后,减压除去冰醋酸并用氯仿溶解残留物,饱和氯化钠水溶液纯化洗涤数次后将有机相分离。有机相中加入无水硫酸镁干燥过夜后,减压除去有机溶剂得到棕色透明油状液体,即制得改性聚硅氧烷A2#(马来酰亚胺化聚硅氧烷A2#);(1) Preparation of modified polysiloxane A2# (maleimidated polysiloxane A2#): The side aminopropyl modified polysiloxane with a weight average molecular weight of 5000 dispersed in 30mL of glacial acetic acid Alkanes and maleic anhydride are placed in the 100mL round-bottomed flask that airway is housed with amino group and maleic anhydride mol ratio as 1:3, amino graft rate 15%, constant pressure low liquid funnel and spherical condenser, in After heating to 160°C under electromagnetic stirring and reflux for 6 hours, the glacial acetic acid was removed under reduced pressure and the residue was dissolved with chloroform, purified and washed several times with saturated aqueous sodium chloride solution, and the organic phase was separated. After adding anhydrous magnesium sulfate to the organic phase and drying it overnight, the organic solvent was removed under reduced pressure to obtain a brown transparent oily liquid, and the modified polysiloxane A2# (maleimidated polysiloxane A2#) was obtained;
(2)改性聚硅氧烷B2#(呋喃乙酰化聚硅氧烷B2#):对50mL圆底烧瓶进行三抽三放后通入氮气进行保护,重均分子量为5000的侧氨丙基改性聚硅氧烷溶于20mL无水乙醚中,氨基接枝率15%,并加入缚酸剂三乙胺,三乙胺添加量为侧氨丙基改性聚硅氧烷质量的5%;在电磁搅拌20min后,将以体积质量比(mL:g)为15:1的溶于有机溶剂四氢呋喃中的呋喃乙酰氯缓慢滴入圆底烧瓶中,其中氨基与呋喃乙酰氯摩尔比为1:3,在回流状态下反应2h后,抽滤去除产生的盐后进行减压蒸馏纯化,获得浅黄色油状液体,即制得改性聚硅氧烷B2#;(2) Modified polysiloxane B2# (furan acetylated polysiloxane B2#): the 50mL round-bottomed flask was pumped three times and discharged three times, and then passed through nitrogen for protection. The side aminopropyl group with a weight average molecular weight of 5000 The modified polysiloxane was dissolved in 20mL of anhydrous ether, the grafting rate of amino group was 15%, and the acid-binding agent triethylamine was added, and the amount of triethylamine added was 5% of the mass of the side aminopropyl modified polysiloxane ; After electromagnetic stirring for 20min, the furoyl chloride dissolved in the organic solvent tetrahydrofuran was slowly dropped into the round-bottomed flask with a volume to mass ratio (mL:g) of 15:1, wherein the molar ratio of amino group to furoyl chloride was 1 :3, after reacting for 2h under the reflux state, carry out vacuum distillation purification after removing the salt produced by suction filtration, obtain light yellow oily liquid, promptly make modified polysiloxane B2#;
(3)有机硅聚合材料2#制备:将马来酰亚胺化聚硅氧烷A2#及呋喃乙酰化聚硅氧烷B2#分别以马来酰亚胺基与呋喃乙酰基计摩尔比为1:2.5溶于有机溶剂二甲苯中,溶剂与原料之间的体积质量比(mL:g)为25:1,并转入圆底烧瓶中,在电磁搅拌下加热至180℃并反应36h,后倒入无水甲醇溶液中,得到浅红色沉淀,抽滤去除溶剂后反复用无水甲醇洗涤数次,真空干燥过夜得有机硅聚合材料2#。(3) Preparation of organosilicon polymer material 2#: Maleimidated polysiloxane A2# and furanacetylated polysiloxane B2# were calculated by maleimide group and furanacetyl group in a molar ratio of 1:2.5 was dissolved in the organic solvent xylene, the volume-to-mass ratio (mL:g) between the solvent and the raw material was 25:1, and transferred into a round bottom flask, heated to 180°C under electromagnetic stirring and reacted for 36h, Then pour it into anhydrous methanol solution to obtain a light red precipitate, remove the solvent by suction filtration, wash with anhydrous methanol several times, and vacuum dry overnight to obtain organosilicon polymer material 2#.
实施例4 包膜肥料2#的制备The preparation of embodiment 4 coated fertilizer 2#
使用实施例3#的有机硅聚合材料2#作为肥料包膜工艺:将尿素用39目的筛子筛分后,分别以50g为一份进行分装;取一份尿素于转鼓包衣机中,调整包衣机角度为40°,转速控制在60r/m,使尿素在包衣机中可以形成连续式料帘;15min后进行预加热,温度控制在约100℃,使尿素颗粒表面呈现微 熔状态,喷入溶于二氯甲烷溶液的有机硅聚合材料2#,有机硅聚合材料2#添加量选取肥料质量的1.5%,包膜过程中通过调节转速防止出现相互粘结情况,使有机硅聚合材料1#在尿素颗粒表面形成均匀的薄膜。Use the organosilicon polymeric material 2# of embodiment 3# as the fertilizer coating process: after the urea is sieved with a 39-purpose sieve, it is divided into parts with 50g; get a part of urea in a drum coating machine, adjust The angle of the coating machine is 40°, and the speed is controlled at 60r/m, so that the urea can form a continuous material curtain in the coating machine; preheat after 15 minutes, and the temperature is controlled at about 100°C, so that the surface of the urea particles is in a slightly molten state , spray into the organosilicon polymer material 2# dissolved in dichloromethane solution, the addition amount of the organosilicon polymer material 2# is selected as 1.5% of the fertilizer mass, and the rotation speed is adjusted during the coating process to prevent mutual adhesion, so that the organosilicon polymerizes Material 1# forms a uniform film on the surface of urea granules.
通过紫外灯下观察有机硅聚合材料在尿素颗粒表面包裹的均匀性。Observe the uniformity of silicone polymer material wrapping on the surface of urea particles under ultraviolet light.
实施例5 自修复的有机硅聚合材料3#的制备Example 5 Preparation of self-healing silicone polymer material 3#
自修复的有机硅聚合材料3#的制备方法包括下述步骤:The preparation method of the organic silicon polymer material 3# of self-healing comprises the following steps:
(1)改性聚硅氧烷A3#(马来酰亚胺化聚硅氧烷A3#)制备:将分散于30mL冰醋酸中的重均分子量为15000的侧氨丙基改性聚硅氧烷和马来酸酐以氨基与马来酸酐摩尔比为1:2.5的量置于装有导气管,氨基接枝率30%,恒压低液漏斗和球形冷凝管的100mL圆底烧瓶中,在电磁搅拌下加热至160℃并回流反应8h后,减压除去冰醋酸并用氯仿溶解残留物,饱和氯化钠水溶液纯化洗涤数次后将有机相分离。有机相中加入无水硫酸镁干燥过夜后,减压除去有机溶剂得到棕色透明油状液体,即制得改性聚硅氧烷A3#(马来酰亚胺化聚硅氧烷A3#);(1) Preparation of modified polysiloxane A3# (maleimidated polysiloxane A3#): The side aminopropyl modified polysiloxane with a weight average molecular weight of 15000 dispersed in 30mL of glacial acetic acid Alkane and maleic anhydride are placed in the 100mL round-bottomed flask of constant pressure low liquid funnel and spherical condenser with airway tube being housed in the amount of 1:2.5 with amino group and maleic anhydride mol ratio, amino grafting rate 30%. After heating to 160°C under electromagnetic stirring and reflux for 8 hours, remove glacial acetic acid under reduced pressure and dissolve the residue with chloroform, purify and wash with saturated sodium chloride aqueous solution several times, and separate the organic phase. After adding anhydrous magnesium sulfate to the organic phase and drying it overnight, the organic solvent was removed under reduced pressure to obtain a brown transparent oily liquid, and the modified polysiloxane A3# (maleimidated polysiloxane A3#) was obtained;
(2)改性聚硅氧烷B3#(呋喃乙酰化聚硅氧烷B3#):对50mL圆底烧瓶进行三抽三放后通入氮气进行保护,重均分子量为15000的侧氨丙基改性聚硅氧烷溶于20mL无水乙醚中,氨基接枝率30%,并加入缚酸剂4-二甲氨基吡啶,4-二甲氨基吡啶添加量为侧氨丙基改性聚硅氧烷B3#质量的5%;在电磁搅拌30min后,将以体积质量比(mL:g)为30:1的溶于有机溶剂二氯甲烷中的呋喃乙酰氯缓慢滴入圆底烧瓶中,其中氨基与呋喃乙酰氯摩尔比为1:5,在回流状态下反应3h后,抽滤去除产生的盐后进行减压蒸馏纯化,获得浅黄色油状液体,即制得改性聚硅氧烷B3#;(2) Modified polysiloxane B3# (furan acetylated polysiloxane B3#): the 50mL round-bottomed flask was pumped three times and released three times, and then passed through nitrogen for protection. The side aminopropyl group with a weight average molecular weight of 15000 The modified polysiloxane was dissolved in 20mL of anhydrous ether, the grafting rate of the amino group was 30%, and the acid-binding agent 4-dimethylaminopyridine was added, and the amount of 4-dimethylaminopyridine added was the 5% of the quality of oxane B3#; after electromagnetic stirring for 30min, the furoyl chloride dissolved in the organic solvent methylene chloride of 30:1 was slowly dropped into the round-bottomed flask with a volume to mass ratio (mL:g), The molar ratio of amino group to furoacetyl chloride is 1:5. After reacting under reflux for 3 hours, remove the generated salt by suction filtration, and carry out distillation and purification under reduced pressure to obtain a light yellow oily liquid, which is the modified polysiloxane B3. #;
(3)有机硅聚合材料3#制备:将马来酰亚胺化聚硅氧烷A3#及呋喃乙酰化聚硅氧烷B3#分别以马来酰亚胺基与呋喃乙酰基计摩尔比为1:3溶于有机溶剂苯甲醇中,溶剂与原料之间的体积质量比为(mL:g)为30:1,并转入圆底烧瓶中,在电磁搅拌下加热至200℃并反应48h,后倒入无水甲醇溶液中,得到浅红色沉淀,抽滤去除溶剂后反复用无水甲醇洗涤数次,真空干燥过夜得有机硅聚合材料3#。(3) Preparation of organosilicon polymer material 3#: Maleimidated polysiloxane A3# and furanacetylated polysiloxane B3# were calculated by maleimide group and furanacetyl group in molar ratio of 1:3 dissolved in the organic solvent benzyl alcohol, the volume-to-mass ratio between the solvent and the raw material (mL:g) is 30:1, and transferred to a round bottom flask, heated to 200°C under electromagnetic stirring and reacted for 48h , and then poured into anhydrous methanol solution to obtain a light red precipitate. After the solvent was removed by suction filtration, it was repeatedly washed with anhydrous methanol several times, and vacuum-dried overnight to obtain organosilicon polymer material 3#.
实施例6 包膜肥料3#的制备The preparation of embodiment 6 coated fertilizer 3#
使用实施例5#的有机硅聚合材料3#作为肥料包膜工艺:将尿素用40目的筛子筛分后,分别以50g为一份进行分装;取一份尿素于转鼓包衣机中,调整包衣机角度为45°,转速控制在80r/m,使尿素在包衣机中可以形成连续式料帘;15min后进行预加热,温度控制在约110℃,使尿素颗粒表面呈现微熔状态,喷入溶于二氯甲烷溶液的有机硅聚合材料3#,有机硅聚合材料3#添加量选取肥料质量的2%,包膜过程中通过调节转速防止出现相互粘结情况,使有机硅聚合材料3#在尿素颗粒表面形成均匀的薄膜。Use the organosilicon polymer material 3# of embodiment 5# as the fertilizer coating process: after the urea is sieved with a 40-mesh sieve, 50g is used as a portion to pack respectively; get a portion of urea in a drum coating machine, adjust The angle of the coating machine is 45°, and the speed is controlled at 80r/m, so that the urea can form a continuous material curtain in the coating machine; preheat after 15 minutes, and the temperature is controlled at about 110°C, so that the surface of the urea particles is in a slightly molten state , spray into the organosilicon polymer material 3# dissolved in dichloromethane solution, the addition amount of the organosilicon polymer material 3# is selected as 2% of the fertilizer mass, and the rotation speed is adjusted during the coating process to prevent mutual adhesion, so that the organosilicon polymerizes Material 3# forms a uniform film on the surface of urea granules.
通过紫外灯下观察有机硅聚合材料在尿素颗粒表面包裹的均匀性。Observe the uniformity of silicone polymer material wrapping on the surface of urea particles under ultraviolet light.
实施例7 包膜肥料1-3#的缓释性能测试Example 7 The slow-release performance test of coated fertilizer 1-3#
分别测试实施例2、4、6分别制得的包膜肥料1-3#的缓释特性,测试方法为水浸泡法。测试结果见图7,由图7可知实施例3相较于1,2具有更好的缓释效果,28天内的累计释放率均未超过80%,已达到缓释肥要求。The slow-release properties of the coated fertilizers 1-3# prepared in Examples 2, 4, and 6 were tested respectively, and the test method was the water soaking method. The test results are shown in Figure 7. It can be seen from Figure 7 that Example 3 has a better slow-release effect than 1 and 2, and the cumulative release rate within 28 days has not exceeded 80%, which has met the requirements of slow-release fertilizers.
分别测试实施例2、4、6分别制得的包膜肥料1-3#的与市售产品养分释放周期(d)、28天累积氮素释放率、包膜材料可修复次数对比见表1。Test the coating fertilizer 1-3# that embodiment 2, 4, 6 makes respectively and commercially available product nutrient release period (d), 28 days cumulative nitrogen release rate, coating material repairable times contrast see table 1 .
表1Table 1
Figure PCTCN2021117481-appb-000008
Figure PCTCN2021117481-appb-000008
由表1可知,本申请制得的包膜肥料缓释速度慢,能够保持养分能够被农作物充分吸收,肥料流失率低,肥料利用率大大提高,从而可以避免过度施用肥料。所制备包膜肥料1#、2#及3#在28天累积氮素释放率上均未超过80%,已达到GB/T 23348-2009要求,其中包膜肥料3#在28天累积氮素释放率上低于1#、2#及市售产品,表明包膜肥料3#缓释效果较好。As can be seen from Table 1, the coated fertilizer prepared by the present application has a slow slow release rate, can maintain nutrients and can be fully absorbed by crops, has a low fertilizer loss rate, and greatly improves the fertilizer utilization rate, thereby avoiding excessive application of fertilizers. The prepared coated fertilizers 1#, 2# and 3# did not exceed 80% of the cumulative nitrogen release rate in 28 days, which has reached the requirements of GB/T 23348-2009, and the coated fertilizer 3# accumulated nitrogen in 28 days The release rate is lower than 1#, 2# and commercially available products, indicating that the slow-release effect of coated fertilizer 3# is better.
图8(A)为制得的包膜肥料1#养分释放后的有机硅复合材料壳表面,由图8(A)可知有机硅复合材料在肥料表面可以形成有孔洞的壳,但随着养分释放之后,可表面出现垮塌,并在周围产生碎屑。图8(B)为包膜肥料3#材料条件处理后发生Diels-Alder逆反应修复后的有机硅复合材料2#壳,由图8(B)可知自修复后有机硅复合材料仍可在肥料表面形成致密保护层,但修复后表面孔洞变多,且孔径变大,意味着本申请中所设计的有机硅复合材料具有一定的自修复次数。Fig. 8(A) is the shell surface of the organosilicon composite material after the nutrient release of the prepared coated fertilizer 1#. It can be seen from Fig. 8(A) that the organosilicon composite material can form a shell with holes on the surface of the fertilizer, but as the nutrients After release, the surface may collapse and create debris around it. Figure 8(B) shows the 2# shell of the organic silicon composite material repaired by the Diels-Alder reverse reaction after the conditioned treatment of the coated fertilizer 3# material. It can be seen from Figure 8(B) that the organic silicon composite material can still be on the surface of the fertilizer A dense protective layer is formed, but the number of pores on the surface becomes larger after repairing, which means that the silicone composite material designed in this application has a certain number of self-repairing times.
实施例8Example 8
按照与实施例1和实施例2的方法不同于表2中的条件分别制得包膜肥料4#-10#和对比包膜材料D1#-D2#,再使用实施例7的测试方法分别测试28天累积氮素释放率和包膜材料可修复次数,结果见表2。According to the conditions different from the method of Example 1 and Example 2 in Table 2, coated fertilizers 4#-10# and contrast coated materials D1#-D2# were respectively tested using the test method of Example 7 The 28-day cumulative nitrogen release rate and the repairable times of the coating material are shown in Table 2.
表2Table 2
Figure PCTCN2021117481-appb-000009
Figure PCTCN2021117481-appb-000009
Figure PCTCN2021117481-appb-000010
Figure PCTCN2021117481-appb-000010
由表2可知,对比包膜肥料D1#重均分子量超过本申请保护范围时,虽与包膜肥料4#、5#相比氮素释放率相差不大,但因可逆取代环己烯结构所占比例较低,使该包膜肥料可修复次数显著降低;对比包膜肥料D2#接枝率超过本申请保护范围内,可逆取代环己烯结构所占比例提升,马来酰亚胺基、呋喃乙酰基交联密度增大,使包膜材料中的空隙密度增加,导致28天累积氮素释放率过高,缓释效果较差。综合来看,分子量、接枝率只有在处于保护范围内时,才能保证所得到的包膜肥料缓释效果好、可修复次数多。As can be seen from Table 2, when the weight-average molecular weight of the coated fertilizer D1# exceeds the protection scope of the present application, although the nitrogen release rate is not much different from the coated fertilizer 4#, 5#, but due to the reversible substitution cyclohexene structure The proportion is low, so that the number of repairs of the coated fertilizer is significantly reduced; the grafting rate of the compared coated fertilizer D2# exceeds the scope of protection of the application, and the proportion of the reversible substitution cyclohexene structure is improved, and the maleimide group, The increase of the cross-linking density of furoacetyl groups increases the void density in the coating material, resulting in a high cumulative nitrogen release rate in 28 days and a poor slow-release effect. On the whole, only when the molecular weight and grafting rate are within the protection range, can the obtained coated fertilizer have good slow-release effect and many repair times.
实施例9Example 9
按照与实施例1和实施例2的方法不同于表3中的条件分别制得包膜肥料11#-和对比包膜材料D2#-,再使用实施例7的测试方法分别测试28天累积氮素释放率和包膜材料可修复次数,结果见表3。Coated fertilizer 11#- and contrast coated material D2#- were prepared respectively according to the conditions different from the method in Example 1 and Example 2 in Table 3, and the test method of Example 7 was used to test the accumulated nitrogen in 28 days respectively Table 3 shows the release rate of the hormone and the number of times the coating material can be repaired.
表3table 3
Figure PCTCN2021117481-appb-000011
Figure PCTCN2021117481-appb-000011
Figure PCTCN2021117481-appb-000012
Figure PCTCN2021117481-appb-000012
由表3可知,对比包膜肥料D3#中,包衣机角度过高或过低均会对氮素释放率产生负面影响,包衣机包衣角度较低时,肥料在包衣机内呈现弧线运动,角度太小时,肥料因离心力不足,下降的速度过快,容易产生因摩擦配装造成的包膜材料分布不均,缓释效果不好,但角度较高时虽然离心力较大,但包膜效果与包膜肥料1#相差不大,但因能耗较高,造成成本增加;对比包膜肥料D4#中,转速的高低同样会对缓释效果产生负面影响,转速较高时,料帘在包衣机中旋转速率较快,包膜材料在肥料表面固化时间较短,在与其他肥料颗粒碰撞时,包膜材料容易从肥料表面脱落或产生缝隙,导致缓释效果差,但转速较低时,包膜材料在肥料表面虽有足够的固化时间,但因速度太慢,包膜效率较低;对比包膜肥料D5#中,随着有机硅聚合材料与肥料颗粒质量比的提升,一方面可以提升包膜液的粘度,使其在肥料表面的黏着力增加,另一方面可以增加包膜液的浓度,使包膜材料在肥料表面的薄膜层厚度增加,这有利于降低28天累积氮素释放率,但欧洲标准委员会对缓释肥料相关规定中指出:在规定时间内,缓释肥养分释放率应不低于75%,虽然包膜肥料D5#中28天累积氮素释放率相比于实施例低,但过低的释放率导致肥料不能在规定的时间内为作物提供充足的养分且不符合缓释肥标准,无法投入缓释肥市场使用。It can be seen from Table 3 that in the comparison of coated fertilizer D3#, the angle of the coating machine is too high or too low will have a negative impact on the nitrogen release rate. When the coating angle of the coating machine is low, the fertilizer will appear in the coating machine. Arc motion, the angle is too small, the fertilizer will fall too fast due to insufficient centrifugal force, and it is easy to cause uneven distribution of coating materials caused by friction fitting, and the slow-release effect is not good, but when the angle is high, although the centrifugal force is greater, However, the coating effect is not much different from that of coated fertilizer 1#, but the cost is increased due to higher energy consumption; compared with coated fertilizer D4#, the speed of rotation will also have a negative impact on the slow-release effect. , the rotation speed of the material curtain in the coating machine is fast, and the curing time of the coating material on the surface of the fertilizer is short. When it collides with other fertilizer particles, the coating material is easy to fall off from the surface of the fertilizer or create gaps, resulting in poor slow-release effect. But when the rotation speed is low, although the coating material has enough solidification time on the fertilizer surface, the coating efficiency is low because the speed is too slow; compared with the coated fertilizer D5#, with the mass ratio of the organic silicon polymer material to the fertilizer particle On the one hand, it can increase the viscosity of the coating liquid, so that its adhesion on the surface of the fertilizer can be increased; Reduce the 28-day cumulative nitrogen release rate, but the European Standards Committee pointed out in the relevant regulations on slow-release fertilizers: within the specified time, the nutrient release rate of slow-release fertilizers should not be less than 75%, although the 28-day accumulation of coated fertilizer D5# The nitrogen release rate is lower than that of the examples, but the low release rate causes the fertilizer to fail to provide sufficient nutrients for the crops within the specified time and does not meet the slow-release fertilizer standard, so it cannot be put into the slow-release fertilizer market for use.
以上所述,仅为本申请的实施例而已,本申请的保护范围并不受这些具 体实施例的限制,而是由本申请的权利要求书来确定。对于本领域技术人员来说,本申请可以有各种更改和变化。凡在本申请的技术思想和原理之内所作的任何修改、等同替换、改进等,均应包含在本申请的保护范围之内。The foregoing is only an embodiment of the application, and the protection scope of the application is not limited by these specific embodiments, but is determined by the claims of the application. For those skilled in the art, various modifications and changes may occur in this application. Any modifications, equivalent replacements, improvements, etc. made within the technical ideas and principles of this application shall be included within the protection scope of this application.

Claims (17)

  1. 一种缓释包膜肥料,其特征在于,其包括肥料颗粒和包覆在所述肥料颗粒外的薄膜,所述薄膜由有机硅聚合材料制得;A slow-release coated fertilizer, characterized in that it includes fertilizer granules and a film coated outside the fertilizer granules, and the film is made of organic silicon polymer material;
    其中,有机硅聚合材料由所述改性聚硅氧烷A和改性聚硅氧烷B发生Diels-Alder反应制得,所述有机聚硅氧烷A在1分子中具有至少一个包含取代烯烃键基团,所述有机聚硅氧烷B在1分子至少具有一个与所述包含取代烯烃键基团发生Diels-Alder反应的包含非芳烃的共轭双烯键基团。Wherein, the organosilicon polymer material is prepared by the Diels-Alder reaction of the modified polysiloxane A and the modified polysiloxane B, and the organopolysiloxane A has at least one substituted olefin in one molecule. The organopolysiloxane B has at least one non-aromatic conjugated diene bond group that undergoes a Diels-Alder reaction with the substituted olefin bond group in one molecule.
  2. 根据权利要求1所述的缓释包膜肥料,其特征在于,所述有机硅聚合材料与所述肥料颗粒的质量比为0.3%-5%。The slow-release coated fertilizer according to claim 1, characterized in that the mass ratio of the organic silicon polymer material to the fertilizer granules is 0.3%-5%.
  3. 根据权利要求2所述的缓释包膜肥料,其特征在于,所述有机硅聚合材料与所述肥料颗粒的质量比为1%-3%。The slow-release coated fertilizer according to claim 2, characterized in that the mass ratio of the organic silicon polymer material to the fertilizer granules is 1%-3%.
  4. 根据权利要求1所述的缓释包膜肥料,其特征在于,所述肥料颗粒的粒径为10~40目。The slow-release coated fertilizer according to claim 1, characterized in that the particle size of the fertilizer particles is 10-40 mesh.
  5. 根据权利要求4所述的缓释包膜肥料,其特征在于,所述肥料颗粒的粒径为20~30目。The slow-release coated fertilizer according to claim 4, characterized in that the particle size of the fertilizer particles is 20-30 mesh.
  6. 根据权利要求1所述的缓释包膜肥料,其特征在于,所述肥料颗粒选自尿素、氮磷钾复合肥、磷酸二铵、中量元素肥、生物肥和有机肥中的至少一种。The slow-release coated fertilizer according to claim 1, wherein the fertilizer particles are selected from at least one of urea, nitrogen, phosphorus and potassium compound fertilizer, diammonium phosphate, medium element fertilizer, biological fertilizer and organic fertilizer .
  7. 根据权利要求1-6中任一项所述的缓释包膜肥料,其特征在于,所述改性聚硅氧烷A中的包含取代烯烃键基团为马来酰亚胺基,所述有机聚硅氧烷B中的所述包含非芳烃的双烯键基团为呋喃乙酰基;The slow-release coated fertilizer according to any one of claims 1-6, wherein the group comprising a substituted olefin bond in the modified polysiloxane A is a maleimide group, and the The non-aromatic dienyl group in organopolysiloxane B is furoacetyl;
    所述改性聚硅氧烷A和改性聚硅氧烷B通过生成至少一个可逆取代环己烯基交联聚合制得所述有机硅聚合材料,所述可逆取代环己烯基的结构如式Ⅰ所示:The modified polysiloxane A and the modified polysiloxane B are cross-linked and polymerized to produce at least one reversible substituted cyclohexenyl group to obtain the silicone polymer material, and the structure of the reversible substituted cyclohexenyl group is as follows: Formula I shows:
    Figure PCTCN2021117481-appb-100001
    Figure PCTCN2021117481-appb-100001
  8. 根据权利要求7所述的缓释包膜肥料,其特征在于,所述改性聚硅氧烷A中的马来酰亚胺基的接枝率X与所述改性聚硅氧烷B中的呋喃乙酰基的接枝率Y之间的比值为1:1.2-1.5;The slow-release coated fertilizer according to claim 7, wherein the graft ratio X of the maleimide group in the modified polysiloxane A is the same as that in the modified polysiloxane B. The ratio between the grafting ratio Y of the furoacetyl group is 1:1.2-1.5;
    所述聚硅氧烷A和所述聚硅氧烷B分别独立的选自聚(二有机硅氧烷)。The polysiloxane A and the polysiloxane B are independently selected from poly(diorganosiloxanes).
  9. 根据权利要求1所述的缓释包膜肥料,其特征在于,所述聚硅氧烷A的结构式如式Ⅱ所示:The slow-release coated fertilizer according to claim 1, wherein the polysiloxane A has a structural formula as shown in Formula II:
    Figure PCTCN2021117481-appb-100002
    Figure PCTCN2021117481-appb-100002
    其中,R 1、R 2、R 3和R 4分别独立的选自烃基、取代烃基、杂芳基、取代杂芳基和非烃类取代基中的一种;m1、n1分别取自>0的整数,式Ⅱ的氨基化聚硅氧烷A的重均分子量为2000~20000,所述氨基化聚硅氧烷A中的氨基的接枝率为3%-30%;所述R 1、R 2、R 3和R 4中的至少一种与式Ⅰ的可逆取代环己烯基的马来酰亚胺基连接; Wherein, R 1 , R 2 , R 3 and R 4 are each independently selected from one of hydrocarbon groups, substituted hydrocarbon groups, heteroaryl groups, substituted heteroaryl groups and non-hydrocarbon substituents; m1 and n1 are respectively selected from >0 is an integer, the weight average molecular weight of the aminated polysiloxane A of formula II is 2,000 to 20,000, and the grafting rate of amino groups in the aminated polysiloxane A is 3%-30%; the R 1 , At least one of R 2 , R 3 and R 4 is connected to the maleimide group of the reversibly substituted cyclohexenyl of formula I;
    所述聚硅氧烷B的结构式分别如式Ⅲ所示:The structural formulas of the polysiloxane B are shown in formula III:
    Figure PCTCN2021117481-appb-100003
    Figure PCTCN2021117481-appb-100003
    其中,R5、R6、R7和R8分别独立的选自烃基、取代烃基、杂芳基、取代杂芳基和非烃类取代基中的一种;m2、n2分别取自>0的整数,式Ⅲ的氨基化聚硅氧烷B的重均分子量为2000~20000,所述氨基化聚硅氧烷B中的氨基的接枝率为3%-30%;所述R5、R6、R7和R8中的至少一种与式Ⅰ的可逆取代环己烯基的呋喃乙酰基相连接。Among them, R5, R6, R7 and R8 are independently selected from one of hydrocarbon groups, substituted hydrocarbon groups, heteroaryl groups, substituted heteroaryl groups and non-hydrocarbon substituents; m2 and n2 are respectively taken from integers>0, the formula The weight average molecular weight of the aminated polysiloxane B of III is 2,000 to 20,000, and the grafting rate of amino groups in the aminated polysiloxane B is 3%-30%; the R5, R6, R7 and R8 At least one of them is connected to the furoacetyl group of the reversibly substituted cyclohexenyl of formula I.
  10. 根据权利要求9所述的缓释包膜肥料,其特征在于,所述R1、R2、R3和R4分别独立的选自烷基;所述R1、R2、R3和R4中的一种与式Ⅰ的可逆取代环己烯基的马来酰亚胺基连接。The slow-release coated fertilizer according to claim 9, wherein said R1, R2, R3 and R4 are independently selected from alkyl groups; one of said R1, R2, R3 and R4 is the same as formula I The maleimido linkage of the reversibly substituted cyclohexenyl group.
  11. 根据权利要求9所述的缓释包膜肥料,其特征在于,所述R5、R6、R7和R8中至少一个选自亚氨基取代烷基,其余为烷基;所述R5、R6、R7和R8中含有的亚氨基与式Ⅰ的可逆取代环己烯基的呋喃乙酰基连接。The slow-release coated fertilizer according to claim 9, wherein at least one of said R5, R6, R7 and R8 is selected from imino-substituted alkyl groups, and the rest are alkyl groups; said R5, R6, R7 and The imino group contained in R8 is connected to the furoacetyl group of the reversibly substituted cyclohexenyl of formula I.
  12. 根据权利要求9所述的缓释包膜肥料,其特征在于,所述R1、R2、R3、R4和,R5、R6、R7和R8中的碳链部分分别独立的选自C1~C5的烷基中的一种。The slow-release coated fertilizer according to claim 9, wherein the carbon chains in R1, R2, R3, R4 and R5, R6, R7 and R8 are independently selected from C1-C5 alkanes one of the bases.
  13. 根据权利要求9所述的缓释包膜肥料,其特征在于,所述R2和R6的分别为丙基和亚氨基取代丙基,所述R3、R4、R5、R7和R8分别为甲基。The slow-release coated fertilizer according to claim 9, wherein said R2 and R6 are respectively propyl and imino substituted propyl, and said R3, R4, R5, R7 and R8 are respectively methyl.
  14. 一种权利要求1-13中任一项所述的缓释包膜肥料的制备方法,其特征在于,其包括下述步骤:A preparation method of the slow-release coated fertilizer according to any one of claims 1-13, characterized in that it comprises the steps of:
    提供具有目标目数的所述肥料颗粒;providing said fertilizer granules having a target mesh;
    提供所述有机硅聚合材料;providing said silicone polymeric material;
    将所述肥料颗粒加入转鼓包衣机中,调整包衣机以35°-45°角度旋转,预热控制肥料颗粒表面微熔;Add the fertilizer granules into the drum coating machine, adjust the coating machine to rotate at an angle of 35°-45°, and preheat to control the micro-melting of the surface of the fertilizer granules;
    将溶于有机溶剂Ⅵ的所述有机硅聚合材料喷到所述肥料颗粒的表面,即 制得所述的缓释包膜肥料。Spray the organosilicon polymer material dissolved in the organic solvent VI onto the surface of the fertilizer granules to obtain the slow-release coated fertilizer.
  15. 根据权利要求14所述的缓释包膜肥料,其特征在于,所述包衣机旋转的速度为40-80r/m;The slow-release coated fertilizer according to claim 14, wherein the speed at which the coating machine rotates is 40-80r/m;
    所述有机硅聚合材料与所述肥料颗粒的质量比为1%-8%。The mass ratio of the organosilicon polymer material to the fertilizer granules is 1%-8%.
  16. 根据权利要求14所述的缓释包膜肥料,其特征在于,所述预热肥料颗粒的温度为80-140℃。The slow-release coated fertilizer according to claim 14, characterized in that the temperature of the preheated fertilizer granules is 80-140°C.
  17. 根据权利要求16所述的缓释包膜肥料,其特征在于,所述预热肥料颗粒的温度为90-110℃。The slow-release coated fertilizer according to claim 16, characterized in that the temperature of the preheated fertilizer granules is 90-110°C.
PCT/CN2021/117481 2021-09-07 2021-09-09 Slow-release coated fertilizer and preparation method therefor WO2023035193A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202111043261.8A CN113831178B (en) 2021-09-07 2021-09-07 Slow-release coated fertilizer and preparation method thereof
CN202111043261.8 2021-09-07

Publications (1)

Publication Number Publication Date
WO2023035193A1 true WO2023035193A1 (en) 2023-03-16

Family

ID=78958529

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2021/117481 WO2023035193A1 (en) 2021-09-07 2021-09-09 Slow-release coated fertilizer and preparation method therefor

Country Status (2)

Country Link
CN (1) CN113831178B (en)
WO (1) WO2023035193A1 (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030040435A1 (en) * 2001-06-05 2003-02-27 Karl Haberle Slow-release fertilizers and method for production of same
CN103755472A (en) * 2014-01-09 2014-04-30 江西省科学院应用化学研究所 Method for preparing sustained-release coating material with organic silicon
CN105111470A (en) * 2015-08-13 2015-12-02 四川大学 Reversible covalent crosslinking polysiloxane elastomer, preparation method therefor and application thereof
JP2016003168A (en) * 2014-06-18 2016-01-12 コニカミノルタ株式会社 Fertilizer particle and method for producing the same
CN105481559A (en) * 2015-12-22 2016-04-13 成都新柯力化工科技有限公司 Preparation method of slow release ecological fertilizer taking organosilicon oligomer as envelope
US20190276376A1 (en) * 2016-05-18 2019-09-12 Basf Se Capsules comprising benzylpropargylethers for use as nitrification inhibitors
WO2019218027A1 (en) * 2018-05-18 2019-11-21 Monash University Core-shell particles
US20210139388A1 (en) * 2018-02-09 2021-05-13 Rynan Technologies Pte Ltd Smart release potash fertilizer granules

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106633555A (en) * 2016-09-14 2017-05-10 同济大学 Polyvinyl alcohol membrane with self-repair function implemented by aid of dynamic covalent bonds and method for preparing polyvinyl alcohol membrane

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030040435A1 (en) * 2001-06-05 2003-02-27 Karl Haberle Slow-release fertilizers and method for production of same
CN103755472A (en) * 2014-01-09 2014-04-30 江西省科学院应用化学研究所 Method for preparing sustained-release coating material with organic silicon
JP2016003168A (en) * 2014-06-18 2016-01-12 コニカミノルタ株式会社 Fertilizer particle and method for producing the same
CN105111470A (en) * 2015-08-13 2015-12-02 四川大学 Reversible covalent crosslinking polysiloxane elastomer, preparation method therefor and application thereof
CN105481559A (en) * 2015-12-22 2016-04-13 成都新柯力化工科技有限公司 Preparation method of slow release ecological fertilizer taking organosilicon oligomer as envelope
US20190276376A1 (en) * 2016-05-18 2019-09-12 Basf Se Capsules comprising benzylpropargylethers for use as nitrification inhibitors
US20210139388A1 (en) * 2018-02-09 2021-05-13 Rynan Technologies Pte Ltd Smart release potash fertilizer granules
WO2019218027A1 (en) * 2018-05-18 2019-11-21 Monash University Core-shell particles

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
FENG, CHEN: "Synthesis of Biomimetic Polymers and Their Applications in Controlled/Slow Release Fertilizer", CHINA MASTER’S THESES FULL-TEXT DATABASE, no. 8, 15 August 2016 (2016-08-15), CN, pages 1 - 91, XP009544416 *
YAN, QIAN: "Preparation and Properties of the Self-healing Silicone Polymer Based on Multiple Reaction", CHINA MASTER’S THESES FULL-TEXT DATABASE, no. 2, 15 February 2020 (2020-02-15), pages 1 - 85, XP009544411 *
YOU SHENGYONG, DAI RUN-YING; LI LING; ZHANG PENG; JIN ZHEN-YU; LE JIN-FENG: "Study on Preparation and Properties of Coating Materials for Slow-release Organosilicon Fertilizer", ACTA AGRICULTURAE JIANGXI, JIANGXI SHENG NONGYE KEXUEYUAN, CN, vol. 30, no. 10, 31 December 2018 (2018-12-31), CN , pages 66 - 70, XP093046611, ISSN: 1001-8581, DOI: 10.19386/j.cnki.jxnyxb.2018.10.14 *

Also Published As

Publication number Publication date
CN113831178B (en) 2023-05-30
CN113831178A (en) 2021-12-24

Similar Documents

Publication Publication Date Title
WO2023035192A1 (en) Self-healing organosilicon polymer material, and preparation method therefor and use thereof
CN106164132B (en) Polyimide compositions
CN108318943B (en) A kind of Responsive photonic crystals elastomeric film material, its preparation and application
Isakova et al. Controlled RAFT polymerization and zinc binding performance of catechol-inspired homopolymers
CN104086761B (en) A kind of waterborne organic silicon modified alkyd resin and preparation method thereof
Li et al. A facile strategy for the fabrication of highly stable superhydrophobic cotton fabric using amphiphilic fluorinated triblock azide copolymers
Arnold et al. Utilizing click chemistry to design functional interfaces through post-polymerization modification
CN103930412B (en) The method preparing polymer, polymer product, biological devices and cyclic carbonate ester
Zhu et al. Polystyrenes with hydrophilic end groups: synthesis, characterization, and effects on the self-assembly of breath figure arrays
Pacini et al. Poly (γ‐glutamic acid) esters with reactive functional groups suitable for orthogonal conjugation strategies
CN104955903B (en) Functional materials with reversible crosslinking
CN104592525B (en) Amphipathic temperature sensitive type poly polypeptide block copolymer molecule brush and its preparation method and application
CN103788368B (en) A kind of aqueous polyamide and its preparation method and application
CN106432656B (en) Preparation method based on the poly- porphyrin of semi-rigid monolithic three dimensional
Simpson et al. Thiol-functionalized poly (ω-pentadecalactone) telechelics for semicrystalline polymer networks
CN106496568A (en) Amphipathic copolymer networks of one kind cleaning anti-soil type and preparation method thereof
CN109666109A (en) Polyethylene glycol-glycidyl methacrylate dissaving polymer and preparation method thereof of epoxy group modification
WO2023035193A1 (en) Slow-release coated fertilizer and preparation method therefor
CN105175750B (en) A kind of preparation method of hydrogel microsphere
Wei et al. Preparation of thermosensitive hydrogels by means of tandem physical and chemical crosslinking
CN108003337B (en) Hyperbranched star polymer of uV curable and its preparation method and application
CN102351984B (en) Biomimetic polymer, and preparation method and application thereof
CN105622788A (en) Three-arm ATRP (atom transfer radical polymerization) initiator with plane conjugated structure, and preparation and application thereof
US5306443A (en) Method for the preparation of conductive polymer film
CN110028639A (en) A kind of photosensitivity Zr-B-Si-C ceramic forerunner and its in-situ preparation method

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 21956378

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE