WO2009070953A1 - Method for preparing microporous mineral fertilizer from silicates rock using hydrothermal chemical reaction - Google Patents
Method for preparing microporous mineral fertilizer from silicates rock using hydrothermal chemical reaction Download PDFInfo
- Publication number
- WO2009070953A1 WO2009070953A1 PCT/CN2008/001185 CN2008001185W WO2009070953A1 WO 2009070953 A1 WO2009070953 A1 WO 2009070953A1 CN 2008001185 W CN2008001185 W CN 2008001185W WO 2009070953 A1 WO2009070953 A1 WO 2009070953A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- potassium
- rock
- mineral fertilizer
- reaction
- water
- Prior art date
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- 239000011707 mineral Substances 0.000 title claims abstract description 100
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims abstract description 98
- 239000011435 rock Substances 0.000 title claims abstract description 96
- 239000003337 fertilizer Substances 0.000 title claims abstract description 91
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 39
- 150000004760 silicates Chemical class 0.000 title abstract 4
- 239000000463 material Substances 0.000 claims abstract description 33
- 239000012190 activator Substances 0.000 claims abstract description 20
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 12
- 238000002156 mixing Methods 0.000 claims abstract description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 45
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 42
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 42
- 239000004571 lime Substances 0.000 claims description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 239000000203 mixture Substances 0.000 claims description 30
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 23
- 239000007795 chemical reaction product Substances 0.000 claims description 22
- 238000004519 manufacturing process Methods 0.000 claims description 21
- 239000010440 gypsum Substances 0.000 claims description 14
- 229910052602 gypsum Inorganic materials 0.000 claims description 14
- 239000000395 magnesium oxide Substances 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 8
- 238000000227 grinding Methods 0.000 claims description 7
- 230000035484 reaction time Effects 0.000 claims description 7
- 229910001593 boehmite Inorganic materials 0.000 claims description 6
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 6
- YLUIKWVQCKSMCF-UHFFFAOYSA-N calcium;magnesium;oxygen(2-) Chemical compound [O-2].[O-2].[Mg+2].[Ca+2] YLUIKWVQCKSMCF-UHFFFAOYSA-N 0.000 claims description 5
- NFMWFGXCDDYTEG-UHFFFAOYSA-N trimagnesium;diborate Chemical compound [Mg+2].[Mg+2].[Mg+2].[O-]B([O-])[O-].[O-]B([O-])[O-] NFMWFGXCDDYTEG-UHFFFAOYSA-N 0.000 claims description 5
- 238000010298 pulverizing process Methods 0.000 claims description 4
- 102000018779 Replication Protein C Human genes 0.000 claims description 2
- 108010027647 Replication Protein C Proteins 0.000 claims description 2
- 239000012254 powdered material Substances 0.000 claims 1
- 239000000843 powder Substances 0.000 abstract description 49
- 239000000126 substance Substances 0.000 abstract description 18
- 239000003999 initiator Substances 0.000 abstract 1
- 230000009466 transformation Effects 0.000 abstract 1
- 235000010755 mineral Nutrition 0.000 description 92
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 91
- 239000011591 potassium Substances 0.000 description 91
- 229910052700 potassium Inorganic materials 0.000 description 91
- 101100399296 Mus musculus Lime1 gene Proteins 0.000 description 38
- 240000006909 Tilia x europaea Species 0.000 description 32
- 238000003756 stirring Methods 0.000 description 21
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 19
- 239000011575 calcium Substances 0.000 description 19
- 239000000047 product Substances 0.000 description 19
- 241000196324 Embryophyta Species 0.000 description 18
- 239000004480 active ingredient Substances 0.000 description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 17
- 238000004090 dissolution Methods 0.000 description 14
- DLHONNLASJQAHX-UHFFFAOYSA-N aluminum;potassium;oxygen(2-);silicon(4+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Al+3].[Si+4].[Si+4].[Si+4].[K+] DLHONNLASJQAHX-UHFFFAOYSA-N 0.000 description 13
- 239000002994 raw material Substances 0.000 description 13
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 12
- 239000004111 Potassium silicate Substances 0.000 description 12
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 12
- 229910052791 calcium Inorganic materials 0.000 description 12
- 239000013078 crystal Substances 0.000 description 12
- 239000011521 glass Substances 0.000 description 12
- NNHHDJVEYQHLHG-UHFFFAOYSA-N potassium silicate Chemical compound [K+].[K+].[O-][Si]([O-])=O NNHHDJVEYQHLHG-UHFFFAOYSA-N 0.000 description 12
- 235000019353 potassium silicate Nutrition 0.000 description 12
- 229910052913 potassium silicate Inorganic materials 0.000 description 12
- 239000010703 silicon Substances 0.000 description 12
- 229910052710 silicon Inorganic materials 0.000 description 12
- 238000004458 analytical method Methods 0.000 description 11
- 239000002689 soil Substances 0.000 description 11
- 239000000243 solution Substances 0.000 description 10
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 9
- 229910052742 iron Inorganic materials 0.000 description 9
- 239000011777 magnesium Substances 0.000 description 9
- 229910052749 magnesium Inorganic materials 0.000 description 9
- 239000010453 quartz Substances 0.000 description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- 240000007313 Tilia cordata Species 0.000 description 8
- 235000015097 nutrients Nutrition 0.000 description 8
- 240000007594 Oryza sativa Species 0.000 description 7
- 235000007164 Oryza sativa Nutrition 0.000 description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 7
- 238000002050 diffraction method Methods 0.000 description 7
- 239000012071 phase Substances 0.000 description 7
- 235000009566 rice Nutrition 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- 239000011573 trace mineral Substances 0.000 description 7
- 235000013619 trace mineral Nutrition 0.000 description 7
- 206010065042 Immune reconstitution inflammatory syndrome Diseases 0.000 description 6
- 239000000404 calcium aluminium silicate Substances 0.000 description 6
- 235000012215 calcium aluminium silicate Nutrition 0.000 description 6
- WNCYAPRTYDMSFP-UHFFFAOYSA-N calcium aluminosilicate Chemical compound [Al+3].[Al+3].[Ca+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O WNCYAPRTYDMSFP-UHFFFAOYSA-N 0.000 description 6
- 229940078583 calcium aluminosilicate Drugs 0.000 description 6
- 239000003814 drug Substances 0.000 description 6
- 238000001228 spectrum Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000011343 solid material Substances 0.000 description 5
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 4
- ZOMBKNNSYQHRCA-UHFFFAOYSA-J calcium sulfate hemihydrate Chemical compound O.[Ca+2].[Ca+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZOMBKNNSYQHRCA-UHFFFAOYSA-J 0.000 description 4
- 230000006378 damage Effects 0.000 description 4
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 239000011572 manganese Substances 0.000 description 4
- 229910052748 manganese Inorganic materials 0.000 description 4
- 229910052863 mullite Inorganic materials 0.000 description 4
- 239000000618 nitrogen fertilizer Substances 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 229910052604 silicate mineral Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 230000035558 fertility Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 229910052900 illite Inorganic materials 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- VGIBGUSAECPPNB-UHFFFAOYSA-L nonaaluminum;magnesium;tripotassium;1,3-dioxido-2,4,5-trioxa-1,3-disilabicyclo[1.1.1]pentane;iron(2+);oxygen(2-);fluoride;hydroxide Chemical compound [OH-].[O-2].[O-2].[O-2].[O-2].[O-2].[F-].[Mg+2].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[K+].[K+].[K+].[Fe+2].O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2 VGIBGUSAECPPNB-UHFFFAOYSA-L 0.000 description 3
- 230000008635 plant growth Effects 0.000 description 3
- 238000000634 powder X-ray diffraction Methods 0.000 description 3
- 229910052761 rare earth metal Inorganic materials 0.000 description 3
- 238000004626 scanning electron microscopy Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 2
- 238000007605 air drying Methods 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910021538 borax Inorganic materials 0.000 description 2
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 2
- OSMSIOKMMFKNIL-UHFFFAOYSA-N calcium;silicon Chemical compound [Ca]=[Si] OSMSIOKMMFKNIL-UHFFFAOYSA-N 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 230000006870 function Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002686 phosphate fertilizer Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000004328 sodium tetraborate Substances 0.000 description 2
- 235000010339 sodium tetraborate Nutrition 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- OBSZRRSYVTXPNB-UHFFFAOYSA-N tetraphosphorus Chemical compound P12P3P1P32 OBSZRRSYVTXPNB-UHFFFAOYSA-N 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- BXVSAYBZSGIURM-UHFFFAOYSA-N 2-phenoxy-4h-1,3,2$l^{5}-benzodioxaphosphinine 2-oxide Chemical compound O1CC2=CC=CC=C2OP1(=O)OC1=CC=CC=C1 BXVSAYBZSGIURM-UHFFFAOYSA-N 0.000 description 1
- 229920000856 Amylose Polymers 0.000 description 1
- 240000007087 Apium graveolens Species 0.000 description 1
- 235000015849 Apium graveolens Dulce Group Nutrition 0.000 description 1
- 235000010591 Appio Nutrition 0.000 description 1
- 240000002791 Brassica napus Species 0.000 description 1
- 240000007124 Brassica oleracea Species 0.000 description 1
- 235000003899 Brassica oleracea var acephala Nutrition 0.000 description 1
- 235000011301 Brassica oleracea var capitata Nutrition 0.000 description 1
- 235000001169 Brassica oleracea var oleracea Nutrition 0.000 description 1
- 235000004977 Brassica sinapistrum Nutrition 0.000 description 1
- 235000002566 Capsicum Nutrition 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 235000019750 Crude protein Nutrition 0.000 description 1
- 244000241257 Cucumis melo Species 0.000 description 1
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 description 1
- 101100136092 Drosophila melanogaster peng gene Proteins 0.000 description 1
- 244000020551 Helianthus annuus Species 0.000 description 1
- 235000003222 Helianthus annuus Nutrition 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 208000002720 Malnutrition Diseases 0.000 description 1
- 244000070406 Malus silvestris Species 0.000 description 1
- 229910019440 Mg(OH) Inorganic materials 0.000 description 1
- 239000006002 Pepper Substances 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 235000016761 Piper aduncum Nutrition 0.000 description 1
- 240000003889 Piper guineense Species 0.000 description 1
- 235000017804 Piper guineense Nutrition 0.000 description 1
- 235000008184 Piper nigrum Nutrition 0.000 description 1
- 244000269722 Thea sinensis Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 244000098338 Triticum aestivum Species 0.000 description 1
- 240000006677 Vicia faba Species 0.000 description 1
- 235000010749 Vicia faba Nutrition 0.000 description 1
- 235000002098 Vicia faba var. major Nutrition 0.000 description 1
- 241000219094 Vitaceae Species 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 240000008866 Ziziphus nummularia Species 0.000 description 1
- FJJCIZWZNKZHII-UHFFFAOYSA-N [4,6-bis(cyanoamino)-1,3,5-triazin-2-yl]cyanamide Chemical compound N#CNC1=NC(NC#N)=NC(NC#N)=N1 FJJCIZWZNKZHII-UHFFFAOYSA-N 0.000 description 1
- WNQQFQRHFNVNSP-UHFFFAOYSA-N [Ca].[Fe] Chemical compound [Ca].[Fe] WNQQFQRHFNVNSP-UHFFFAOYSA-N 0.000 description 1
- JOOKTTKZGRVHOQ-UHFFFAOYSA-N [Ca].[K].[Si] Chemical compound [Ca].[K].[Si] JOOKTTKZGRVHOQ-UHFFFAOYSA-N 0.000 description 1
- KMNWCNNLFBCDJR-UHFFFAOYSA-N [Si].[K] Chemical compound [Si].[K] KMNWCNNLFBCDJR-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 235000021016 apples Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000021329 brown rice Nutrition 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000004683 dihydrates Chemical class 0.000 description 1
- 238000007922 dissolution test Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 235000020774 essential nutrients Nutrition 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 229910052631 glauconite Inorganic materials 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 235000021021 grapes Nutrition 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000001071 malnutrition Effects 0.000 description 1
- 235000000824 malnutrition Nutrition 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000000386 microscopy Methods 0.000 description 1
- 239000010811 mineral waste Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000005445 natural material Substances 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 208000015380 nutritional deficiency disease Diseases 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 231100000915 pathological change Toxicity 0.000 description 1
- 230000036285 pathological change Effects 0.000 description 1
- 238000004181 pedogenesis Methods 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
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- 238000005245 sintering Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
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- 239000002912 waste gas Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004876 x-ray fluorescence Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
Definitions
- the invention belongs to the field of mineral fertilizer production, and particularly relates to a method for preparing multi-element microporous mineral fertilizer from silicate rock by hydrothermal chemical reaction in a semi-wet state. Background technique
- Plant growth requires not only NPK, but also medium elements such as silicon, calcium, magnesium, and sulfur, as well as trace elements such as iron, manganese, boron, and rare earth.
- medium elements such as silicon, calcium, magnesium, and sulfur, as well as trace elements such as iron, manganese, boron, and rare earth.
- trace elements such as iron, manganese, boron, and rare earth.
- Each of the essential nutrients has its special function and cannot be Replaced by other elements.
- the various fertility factors in the soil are not isolated, but interconnected and mutually constrained.
- the yield of crops depends mainly on the supply of the least amount of nutrients in the soil (similar to the barrel theory, the storage capacity of the barrel depends on the twist of the shortest board), and the elements such as potassium, silicon, calcium and magnesium in the soil.
- the shortage seriously restricts the absorption and utilization of nitrogen and phosphorus by crops.
- maintaining a nutrient balance is a key factor for a sustainable agricultural farming system.
- the existing hydrothermal chemical methods mainly include the following methods.
- GB186199 discloses a method for extracting potassium from feldspar.
- the potassium-containing rock is ground into a fine powder in a ball mill or a roller mill, and then the potassium-containing rock fine powder and the dilute hydrochloric acid solution are mixed and placed in an acid-resistant colloid mill. Grinding into a high-fine suspension, and transferring the obtained high-fineness suspension to the autoclave, heat treatment at about 225 ° C (25 atm), a large amount of potassium in the potassium-containing rock is dissolved into the solution, and filtered. , Evaporation and concentration, KC1 can be obtained.
- the potassium-containing rock fine powder may also be mixed with an alkali solution, processed into a fine-grained suspension in a colloid mill, and then heat-treated in an autoclave, filtered, and concentrated by evaporation to obtain a KOH product.
- Jumei Yamasaki conducted a high-pressure extraction of potassium from potassium feldspar with Ca(OH) 2 slurry at 100 ° C to 400 ° C.
- the potassium leaching rate was 90% ( Jumei Yamasaki. J. Chem.Soc. Japan Ind Chem Sect.
- Chemak found that at 150 °C ⁇ 200 °C, the KOH solution reacted with the shale in the Opalinus region of Switzerland to form calcium cross zeolite, which on the one hand activated potassium in the shale and on the other hand because the potassium ions were in the zeolite.
- the cavity and channel are not filtered by water, and a long-acting potash can be prepared (JA Chermak.
- Potassium feldspar powder is placed in a 300 ⁇ high pressure alkaline water system to dissociate the ore to obtain AI(OH) 3 and KOH solutions.
- the inventors have also carried out research on extracting potassium from potassium-containing silicate rock (insoluble potassium ore) since 1996. Research, has won three invention patents (patent number ZLO 1100474.6, ZL01100475.4 and ZL02156824.3) 0 on the basis of learning from domestic and foreign experience in potassium, created a new hydrothermal chemical reaction method to extract potassium, KOH, K 2 C0 3 and K 2 S0 4 preparations were obtained.
- the potassium-containing silicate rock used is mainly a special type of rock composed of authigenic silicate minerals. In this type of rock, the potassium-bearing minerals are mainly potassium feldspar, illite, glauconite, mica minerals, etc.
- the chemical composition has a high K 2 0 content, generally more than 10%.
- the potassium-containing silicate rock used in the prior art is mainly a special rock composed of autogenous silicate minerals having a relatively high content of ⁇ 2 ⁇ , and there is no method for producing mineral fertilizer by using ordinary silicate rock. . More importantly, to date, there has not been an effective nutrient that can simulate the geochemical weathering process, transform the various minerals in silicate rock into plant growth, and make it unique. Structural technology. Summary of the invention
- the object of the present invention is to provide a hydrothermal chemical reaction method capable of converting a main element and a trace element in a silicate rock into a multi-element novel mineral fertilizer which can be absorbed by a plant.
- reaction product is dried, pulverized and sieved to obtain a multi-element microporous mineral fertilizer.
- the alkaline earth activators described therein include lime, light burned magnesia and dolomitic lime.
- the second solution adopted by the present invention to solve the technical problem is: using a hydrothermal chemical reaction to prepare a multi-element microporous mineral fertilizer from a silicate rock, the characteristics of which include the following steps: (1) pulverizing and grinding the silicate rock, the alkaline earth activator and the activator into a powdery material;
- reaction product is dried, pulverized and sieved to obtain a multi-element microporous mineral fertilizer.
- the alkaline earth activator described therein includes lime, light burned magnesia and dolomitic lime, and the activator comprises gypsum and magnesium borate.
- Multi-element microporous mineral fertilizer prepared from a potassium-containing silicate rock according to the method provided by the present invention, comprising
- the invention transforms the main elements and trace elements in the silicate rock into a multi-mineral mineral fertilizer which can be absorbed by the plant, and reforms the concept of the traditional single element fertilizer or the simple element compound fertilizer.
- the method for preparing a multi-element mineral fertilizer of the present invention can rapidly and cost-effectively convert various minerals in a silicate rock into an effective form that the plant can absorb, thereby possibly ending the human being at the root. It has historically relied on the natural weathering process to obtain the state of effective mineral nutrients in the soil.
- Figure 1 is an X-ray powder crystal diffraction phase analysis diagram of a hydrothermal reaction product
- Figure 2 is a scanning electron micrograph of a hydrothermal reaction product. detailed description
- the silicate rock used for producing the mineral fertilizer is not particularly limited in the present invention, and complicated pre-treatment such as beneficiation, roasting, and the like is not required.
- the alkaline earth activator used in the present invention may be either a relatively pure industrial lime or an industrial light burned magnesia, or a dolomitic lime obtained by calcination of dolomite, wherein CaO-MgO may be in any ratio.
- the activator used in the present invention may be either gypsum or magnesium borate.
- the presence of gypsum The activity of Ca(OH) 2 or/and Mg(OH) 2 is greatly stimulated, resulting in higher conversion.
- Magnesium borate can promote the disintegration and destruction of the silicon oxytetrahedron and the aluminoxy tetrahedron structure in the silicate mineral, thereby achieving the purpose of increasing the conversion rate and increasing the content of the active ingredient in the product.
- the particle size of the solid material is selected to be less than 200 mesh (i.e., 0.074 mm or less). Excessive particle size affects the rate of reaction, resulting in a decrease in the amount of active ingredient in the product. The particles should not be too fine, otherwise the power consumption in the grinding will increase, resulting in an increase in production costs.
- the amount of water is extremely important. Too little water does not guarantee the dissolution of the various components, while too much water reduces the throughput of the material, thereby reducing productivity.
- the amount of water used in the present invention is selected in accordance with the amount of the solid material so that the solid material is in a semi-wet state.
- the ratio of the amount of water to the solid material i.e., the solid-liquid ratio, is 1:1 to 3, preferably 1:1.2 to 1.5.
- the pressure in the reaction system is also important for the hydrothermal reaction.
- steam can be introduced into the reaction system to keep the reaction pressure constant.
- the greater the pressure the more favorable the hydrothermal reaction is.
- the pressure of the introduced vapor is preferably 0.2 to 5 MPa, more preferably 0.5 to 2 MPa, and most preferably about 1.2 to 1.3 MPa.
- the reaction temperature and time are important factors in determining the effect of the hydrothermal reaction.
- the higher temperature facilitates the disintegration and destruction of the potassium-containing silicate in the hydrothermal chemical reaction, thereby achieving the purpose of increasing the conversion rate and increasing the content of the active ingredient in the product, and also shortening the reaction time and increasing the productivity.
- the excessively high reaction temperature requires higher and stricter heat resistance and pressure resistance performance of the reactor, resulting in an increase in equipment investment, which is not conducive to reducing production costs.
- lower temperatures result in lower conversion rates, lower levels of active ingredients in the product, and excessive reaction times, increasing production costs.
- the reaction temperature range of the present invention is preferably from 100 to 300 ° C, more preferably from 130 to 250 ° C, most preferably from 170 to 200 ° C, from the viewpoint of obtaining an ideal multi-element mineral fertilizer and reducing cost, and the reaction time is preferably It is 5 to 24 hours, more preferably 7 to 14 hours.
- the hydrothermal reaction of the present invention is carried out under static conditions, which can greatly reduce energy consumption, make the technology simple, and is easy to implement in the process flow, and the worker is easy to operate and implement. Moreover, there is no discharge of waste water, waste gas and solid waste in the whole production process, which is a green environmental protection technology.
- the results of the dissolution test on the hot water reaction product according to the procedures prescribed by the Ministry of Agriculture indicate that 65%-95% of the solid phase material composition can be dissolved in 0.5 mole hydrochloric acid solution, which is a water-soluble substance that can be absorbed by plants. Or hydrazine soluble components.
- the water-soluble and hydrazine-soluble K 2 0 content is about 4%-6% (equivalent to the potassium and calcium fertilizer currently on the market), and is a chlorine-free potassium fertilizer.
- this product is a good long-acting slow-release mineral fertilizer with potassium, silicon, calcium, magnesium, iron, manganese and boron.
- the multi-element mineral fertilizer of the present invention is mainly composed of fine crystals of the following two synthetic minerals: Tobe mullite [Ca 5 Si 6 0 16 (OH) 2 .43 ⁇ 40] and hydrated calcium aluminosilicate [Ca 3 Al 2 (Si0 4 )(OH)
- Figure 2 shows the results of scanning electron microscopy analysis of the multi-element mineral fertilizer of the present invention.
- the particles of the new type of mineral fertilizer are very fine, and are nano-submicron; wherein the hydrated calcium aluminosilicate is micron-sized granules (particle size 1-5 microns).
- the tobemorite stone is in the form of nano-scale flakes (the thickness of the flakes is tens to hundreds of nanometers).
- the mineral fertilizer also shows a highly developed microporous structure under a scanning electron microscope, so the mineral fertilizer has a loose texture and a bulk density of only 0.70-0.80 g/cm 3 , so it is also called a microporous mineral fertilizer. Due to the unique fine particles and microporous structure of the mineral fertilizer, it has very high activity, which greatly improves its ability to be dissolved and absorbed by the plant root acid. Moreover, the unique microporous structure of this product also has the functions of retaining water and ensuring fertilizer, improving soil aggregate structure, and promoting ventilation and ventilation of plant roots.
- the unique fine-grained and microporous structure of this mineral fertilizer is due to the use of a unique alkaline earth activator and a semi-wet process during its preparation, and the temperature, pressure and hydrothermal reaction are controlled just right. time.
- the potassium silicon calcium fertilizer produced by the roasting process, the yellow phosphorus slag produced by the phosphating plant, and the silicon calcium fertilizer produced by the steel slag of the steel enterprise do not have such a microporous structure under the scanning electron microscope, and the X-ray powder crystal Diffraction phase analysis shows that it is amorphous or cryptocrystalline.
- the multi-element microporous mineral fertilizer of the invention does not contain any harmful substances, and retains the natural material composition characteristics of the silicate rock itself. Like the soil formed by natural weathering, the farmland does not cause extratoxicity and pollution after application, and is suitable for Produce natural green food. Moreover, the multi-element microporous mineral fertilizer product of the invention can not cause agricultural non-point source pollution as a long-acting slow-release fertilizer.
- Potassium-containing silicate rock from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows
- X-ray powder crystal diffraction analysis indicates that the potassium-containing rock is mainly potassium feldspar, and the other is quartz.
- Lime Contains 97% of CaO (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
- Potassium-containing silicate rock from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows
- X-ray powder crystal diffraction analysis indicates that the potassium-containing rock is mainly potassium feldspar, and the other is quartz.
- Lime Contains 97% of Ca0 (chemically pure, purchased from China Pharmaceuticals Beijing Supply Station).
- Gypsum From the Xinjiang and Buxail County Xiazizi bentonite mining area, for the crystallized transparent gypsum, heated in a laboratory oven for 120 hours to obtain hemihydrate gypsum (CaS0 4 ⁇ 1/2H 2 0).
- the obtained product was transferred to a filter, and the soluble potassium was extracted with water.
- 100 ml of potassium-containing filter solution was obtained. After dilution, the concentration of potassium in the liquid sample was measured by a flame photometer. The measurement result was converted into a K 2 0 concentration of 5080 mg/L 5.000 g of potassium-containing rock ore powder containing K 2 0 639.5 mg.
- the leachate is equivalent to a K 20 concentration of 5080 mg/l
- 100 ml of the filtrate contains K 2 0 508.0 mg, and therefore, the dissolution rate of potassium in the potassium-containing mineral is 79.44%.
- Example 3 Comparing Example 1 and Example 2, it can be seen that a certain amount of gypsum (herely hemihydrate gypsum) was added to the formulation, which stimulated the activity of lime, and the dissolution rate of potassium in the potassium-containing rock was increased by 8.45%.
- gypsum hereinafter hemihydrate gypsum
- Potassium-containing silicate rock taken from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows:
- X-ray powder crystal diffraction analysis indicates that the silicate rock mineral composition is mainly potassium feldspar, and the others are quartz.
- Lime Contains 97% of CaO (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
- silicate rock and lime are respectively ground to below 200 mesh to obtain silicate rock powder and lime powder; 15 ml of water is added to the plastic vessel, and then 5.700 g of silicate rock powder and 4.300 g of lime powder are added. Add to the vessel in turn, and stir to mix the materials evenly; (2) The plastic vessel containing the sample is placed in an autoclave and reacted at 191 ° C for 8 hours;
- Potassium-containing silicate rock from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows;
- X-ray powder crystal diffraction analysis indicated that the potassium-bearing rock mineral composition is mainly potassium feldspar, and the others are quartz.
- Light burned boehmite ore The original ore sample was obtained from Liaoning Tiancheng Chemical Plant, and the raw ore coarse crushed sample was placed in a muffle furnace. At 70 (TC heating and constant temperature for 0.5 hour, it was taken out to obtain a light phase dominated by the glass phase. Burning magnesia ore.
- Potassium-containing silicate rock taken from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows:
- X-ray powder crystal diffraction analysis indicated that the potassium-bearing rock mineral composition is mainly potassium feldspar, and the others are quartz.
- Potassium-containing silicate rock taken from Nanshan, Miyun County, Beijing, its chemical composition (%> is as follows:
- X-ray powder crystal diffraction analysis indicated that the potassium-bearing rock mineral composition is mainly potassium feldspar, and the others are quartz.
- Potassium-rich rock taken from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows:
- X-ray powder diffraction analysis indicates that the potassium-rich rock mineral composition is mainly potassium feldspar, and the others are quartz.
- Baiyun Lime Containing 53.23 % of CaO, 36.27% of MgO, and 8.07% loss on ignition, taken from the Babaoshan limestone mine in Huailai County, Hebei province.
- Semi-hydrated gypsum purchased from the market.
- the maximum conversion rate of the insoluble potassium in the raw material to soluble potassium can reach 95.91%.
- Potassium-containing silicate rock ⁇ from Xuanhua, Zhangjiakou City, Hebei province, its chemical composition (%) is as follows:
- X-ray powder diffraction analysis indicates that the mineral composition is mainly potassium feldspar and illite, and the others are quartz.
- Lime Containing 84% CaO, containing Mg0 3%, produced by Xuanhua Iron and Steel Company Longyang Calcium Plant.
- Gypsum Dihydrate gypsum, purchased from Xuanhua Building Materials Store.
- Potassium-containing silicate rock ⁇ from Xuanhua, Zhangjiakou City, Hebei province, chemical composition (%) is as follows:
- X-ray powder diffraction analysis indicates that the mineral composition is mainly potassium feldspar and illite, and the others are quartz.
- Lime Contains 84% of Ca0, contains 3% of Mg0, and is produced by Xuanhua Iron and Steel Company Longyang Calcium Plant.
- Light burned boehmite The ore sample was obtained from Liaoning Tiancheng Chemical Plant. The crude ore sample was placed in a muffle furnace, heated at 700 °C for 0.5 hour, and taken out to obtain a glass-based light burn. Boraxite ore.
- test results are as follows:
- Table 8 Main element content (wt%) of the multi-element microporous mineral fertilizer of Example 8.
- Table 9 Trace element content (mg/k g , ie ppm) of the multi-element microporous mineral fertilizer of Example 8.
- Component B Ba Cd Co Cr Cu Mo Ni Pb Sr V Zn Content 559.0 262.4 3.85 10.15 58.65 5.85 10.15 53.95 10.15 216.85 141.75 81.5
- microporous mineral fertilizer Scanning electron microscopy (LE01450VP type, produced by Leo, Germany) was used to observe and analyze the microstructure of mineral fertilizers. It was found that the two main synthetic minerals of microporous mineral fertilizers are nano-submicron-sized fine particles. One is spherical (hydrated calcium aluminosilicate), the other mineral is flaky (tobe mullite), and a large number of micropores are distributed (see Figure 2), so it is called microporous mineral fertilizer.
- the bulk specific gravity of the new microporous mineral fertilizer was determined by the conventional volumetric flask method and found to be 659 g/1 or 0.659 g/cm3. Obviously, its specific gravity is small, which is consistent with the large number of micropore distributions observed in SEM microscopic observations.
- Example 8 Active ingredient of multi-element microporous mineral fertilizer (%) Table 11 Effective trace element content (mg/kg, ie ppm) of the multi-element microporous mineral fertilizer of Example 8.
- Component B Ba Cd Co Cr Mo Ni Pb Sr V Zn Cu Contains a 458.70 78.70 0.20 2.90 23.10 2.90 30.30 2.90 211.89 94.30 18.20 0.00
- the multi-element microporous mineral fertilizer prepared from silicate rock using the hydrothermal chemical reaction of the present invention contains about 4% to 6% of water-soluble and hydrazine-soluble K 2 0 (equivalent to a chlorine-free potassium fertilizer).
- this product is a good multi-element sustained-release long-acting mineral fertilizer such as potassium, silicon, calcium, magnesium, iron, manganese and boron.
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Abstract
The invention provides a method for preparing microporous mineral fertilizer from silicates rock using hydrothermal chemical reaction, characterized in mixing silicates rock powder, solonetz initiator powder and activator powder and making hydrothermal reaction under subhumid condition. The mineral substances contained in silicates rock can be converted to active forms which are easily absorbed by plants, with transformation rates of 65-95%. The multiplex material fertilizer produced by such method has special microporous structure.
Description
利用水热化学反应由硅酸盐岩石制取多元素微孔矿物肥料的方法 Method for preparing multi-element microporous mineral fertilizer from silicate rock by hydrothermal chemical reaction
技术领域 Technical field
本发明属于矿物肥料生产领域, 特别涉及到一种在半湿状态下利用水热化学反应 由硅酸盐岩石制取多元素微孔矿物肥料的方法。 背景技术 The invention belongs to the field of mineral fertilizer production, and particularly relates to a method for preparing multi-element microporous mineral fertilizer from silicate rock by hydrothermal chemical reaction in a semi-wet state. Background technique
植物生长不仅需要氮磷钾, 还需要硅、 钙、 镁、 硫等中量元素以及铁、 锰、 硼、 稀土等微量元素, 而且每一种必需的营养元素都有其特殊的功能, 不能被其它元素所 代替。 Plant growth requires not only NPK, but also medium elements such as silicon, calcium, magnesium, and sulfur, as well as trace elements such as iron, manganese, boron, and rare earth. Each of the essential nutrients has its special function and cannot be Replaced by other elements.
土壤中的各种肥力因素不是孤立的, 而是相互联系和相互制约的。 根据最小养分 定律, 农作物的产量主要取决于土壤中数量最少的养分的供应量 (类似于木桶理论, 木桶的贮水量取决于最短木板的髙度), 土壤中钾硅钙镁等元素的短缺严重制约了农 作物对氮磷的吸收利用。 显然, 对于一个可持续的农业耕作系统, 保持养分平衡是一 个关键因子。 The various fertility factors in the soil are not isolated, but interconnected and mutually constrained. According to the law of minimum nutrient, the yield of crops depends mainly on the supply of the least amount of nutrients in the soil (similar to the barrel theory, the storage capacity of the barrel depends on the twist of the shortest board), and the elements such as potassium, silicon, calcium and magnesium in the soil. The shortage seriously restricts the absorption and utilization of nitrogen and phosphorus by crops. Clearly, maintaining a nutrient balance is a key factor for a sustainable agricultural farming system.
但长期以来, 不平衡施肥的问题十分突出, 过量施用氮肥, 而钾硅钙镁铁锰等矿 物质养分很少得到补充, 长期的高产使土壤中的钾硅以及其它元素被大量消耗, 土壤 肥力的协调平衡被打破, 综合肥力不断下降。 However, for a long time, the problem of unbalanced fertilization is very prominent. Excessive application of nitrogen fertilizer, while mineral nutrients such as potassium, silicon, calcium, magnesium, iron and manganese are rarely supplemented. Long-term high yields cause large amounts of potassium, silicon and other elements in the soil to be consumed. The coordination balance has been broken and the overall fertility has been declining.
土壤肥力失衡的后果是, 1 ) 氮、 磷肥的实际利用率很低, 氮肥不足 30%, 这不 仅限制了农业的进一步增产, 而且提高了农业生产成本, 还造成农业立体污染; 2) 钾硅钙镁硫等品质元素的短缺引发营养失调, 不仅植物易发生病变, 而且农产品的品 质下降, 如瓜不香、 果不甜; 3 ) 过量施用氮肥一方面造成土壤酸化、 次生盐渍化, 有害生物滋生, 同时还容易造成农产品中的硝酸盐残留超标。 The consequences of soil fertility imbalance are: 1) the actual utilization rate of nitrogen and phosphate fertilizer is very low, and the nitrogen fertilizer is less than 30%, which not only limits the further increase of agricultural production, but also increases the agricultural production cost and also causes three-dimensional pollution of agriculture; 2) Potassium silicon The shortage of quality elements such as calcium, magnesium and sulfur causes malnutrition, not only plants are prone to pathological changes, but also the quality of agricultural products is degraded, such as melon is not fragrant, fruit is not sweet; 3) excessive application of nitrogen fertilizer on the one hand causes soil acidification, secondary salinization, Pests breed, and at the same time, it is easy to cause nitrate residues in agricultural products to exceed the standard.
因此, 迫切需要一种有效的多元素矿物肥料, 该多元素矿物肥料能够被植物有效 吸收, 并且全面补充植物生长所需的各种养分。 Therefore, there is an urgent need for an effective multi-element mineral fertilizer which can be effectively absorbed by plants and fully supplements various nutrients required for plant growth.
我们知道, 土壤是由岩石通过自然界的地球化学风化成土过程转化而成的, 以质 量计, 土壤固相物质的约 95%是由岩石风化而来的各种矿物质所组成。 然而, 这些矿 物质绝大部分是以植物不可吸收的形态存在, 只有极少一部分(3%-8%)在风化成土 过程中被转化成了能够被植物所吸收的有效营养成分。 正是这一小部分有效的矿物质
养分, 使得土壤能够生长植物。 We know that the soil is transformed from the rock through the geochemical weathering process of nature. About 95% of the soil solid matter is composed of various minerals derived from the weathering of the rock. However, most of these minerals are in a form that is not absorbable by plants, and only a very small fraction (3%-8%) is converted into an effective nutrient that can be absorbed by plants during weathering. It’s this small part of the effective minerals. Nutrients that allow the soil to grow plants.
但是, 自然成土过程漫长 (数千 -数万年), 而且转化率很低。 因此人们一直尝试 将硅酸盐岩石中的各种矿物质高效且大比例地转化成为植物可以吸收的有效形态。 与 此有一定关联的前期工作可以大致概括为以下三个方面: 1、 将含钾硅酸盐岩石 (又 被称为不溶性钾矿) 中的非水溶性钾转化为可溶性钾并开发出钾肥; 2、 利用炼铁废 渣、 黄磷废渣等幵发硅钙肥等矿物肥料; 3、 将碳酸盐岩石焙烧成石灰作钙镁肥用。 其中, 由含钾硅酸盐岩石提取可溶性钾研究得最多。 However, the natural process of soil formation is long (thousands - tens of thousands of years), and the conversion rate is very low. Therefore, attempts have been made to efficiently and extensively convert various minerals in silicate rock into effective forms that plants can absorb. The preliminary work related to this can be roughly summarized as the following three aspects: 1. Converting water-insoluble potassium in potassium-containing silicate rock (also known as insoluble potassium ore) into soluble potassium and developing potassium fertilizer; 2. Using mineral waste such as iron-calcium waste and yellow phosphorus waste residue, etc.; 3. Calcining carbonate rock into lime for calcium and magnesium fertilizer. Among them, the extraction of soluble potassium from potassium-containing silicate rocks was the most studied.
目前利用含钾硅酸盐岩石制取钾肥的方法, 归纳起来主要有三种, 即煅烧法或烧 结法、 水热化学法、 微生物法。 其中现有的水热化学法主要包括如下方法。 At present, there are mainly three methods for preparing potassium fertilizer using potassium silicate rock, namely, calcination method or sintering method, hydrothermal chemical method, and microbial method. Among them, the existing hydrothermal chemical methods mainly include the following methods.
GB186199公开了一种从长石中提取钾的方法, 首先在球磨机或滚筒磨机中将含 钾岩石研磨成细粉, 然后将含钾岩石细粉及稀盐酸溶液混合置于耐酸的胶体磨中研磨 成高细度悬浮物, 再把得到的高细度悬浮物转移至髙压釜中, 在大约 225'C (25大气 压)加热处理, 含钾岩石中大量的钾被溶入溶液中, 过滤, 蒸发浓缩, 可获得 KC1。 含钾岩石细粉也可以与碱溶液混合, 在胶体磨中加工成高细度悬浮物, 然后再在高压 釜中加热处理, 再经过滤, 蒸发浓缩, 制得 KOH产品。 GB186199 discloses a method for extracting potassium from feldspar. First, the potassium-containing rock is ground into a fine powder in a ball mill or a roller mill, and then the potassium-containing rock fine powder and the dilute hydrochloric acid solution are mixed and placed in an acid-resistant colloid mill. Grinding into a high-fine suspension, and transferring the obtained high-fineness suspension to the autoclave, heat treatment at about 225 ° C (25 atm), a large amount of potassium in the potassium-containing rock is dissolved into the solution, and filtered. , Evaporation and concentration, KC1 can be obtained. The potassium-containing rock fine powder may also be mixed with an alkali solution, processed into a fine-grained suspension in a colloid mill, and then heat-treated in an autoclave, filtered, and concentrated by evaporation to obtain a KOH product.
Jumei Yamasaki曾进行过 100°C〜400°C条件下以 Ca(OH)2浆液高压萃取钾长石中 的钾的研究, 钾的浸出率为 90% ( Jumei Yamasaki. J. Chem.Soc. Japan Ind Chem Sect.Jumei Yamasaki conducted a high-pressure extraction of potassium from potassium feldspar with Ca(OH) 2 slurry at 100 ° C to 400 ° C. The potassium leaching rate was 90% ( Jumei Yamasaki. J. Chem.Soc. Japan Ind Chem Sect.
1951, 54(1): 704)。 Chemak发现, 在 150°C〜200°C时, KOH溶液与瑞士 Opalinus地 区页岩反应, 可生成钙十字沸石, 一方面使页岩中钾得到活化, 另一方面由于钾离子 处在沸石的空腔和通道中又不致于被水所淋滤, 可制得一种长效钾肥(J. A. Chermak.1951, 54(1): 704). Chemak found that at 150 °C ~ 200 °C, the KOH solution reacted with the shale in the Opalinus region of Switzerland to form calcium cross zeolite, which on the one hand activated potassium in the shale and on the other hand because the potassium ions were in the zeolite. The cavity and channel are not filtered by water, and a long-acting potash can be prepared (JA Chermak.
Clays and clay Miner. 1993, 41(3): 365-372 )。 东南大学蓝计香及华东理工大学颜勇捷 (蓝计香, 颜勇捷, [J], 髙技术通讯, 1994, 8: 26-28) 研究了消石灰和钾长石的加 压反应条件, 反应是在 FYX05A型永磁搅拌式高压反应釜中进行, 容积 0.5升, 最高 工作温度 350°C, 工作压力 200atm, 搅拌速度 50〜1000rpm, 钾长石的钾浸取率可达 90%或更高。 该浸取方法的缺点在于实施动态搅拌, 水与固料比较大 (最低不能小于Clays and clay Miner. 1993, 41(3): 365-372). Lan Jixiang from Southeast University and Yan Yongjie from East China University of Science and Technology (Lan Jixiang, Yan Yongjie, [J], 髙Technical Communication, 1994, 8: 26-28) studied the pressurized reaction conditions of slaked lime and potassium feldspar. The reaction is carried out in a FYX05A permanent magnet stirred high pressure reactor with a volume of 0.5 liter, a maximum working temperature of 350 ° C, a working pressure of 200 atm, a stirring speed of 50 to 1000 rpm, and a potassium leaching rate of potassium feldspar of 90% or more. high. The disadvantage of this leaching method is that dynamic stirring is carried out, and water and solid materials are relatively large (minimum can not be less than
8), 电能消耗大, 其设备密封性严, 造价高。 8), the power consumption is large, the equipment is tightly sealed and the cost is high.
中南大学赵恒勤等人(赵恒勤, 胡宠杰, 马化龙等, [J] 中国锰业, 2003 , 20(1): Zhao Hengqin and others from Central South University (Zhao Hengqin, Hu Petjie, Ma Hualong, et al. [J] China Manganese Industry, 2003, 20(1):
27-29)将钾长石粉置于 300Ό高压碱水体系中, 可使矿石解离得到 AI(OH)3和 KOH 溶液。 27-29) Potassium feldspar powder is placed in a 300 Ό high pressure alkaline water system to dissociate the ore to obtain AI(OH) 3 and KOH solutions.
本发明人自 1996年以来也开展了从含钾硅酸盐岩石(不溶性钾矿)中提取钾的研
究,先后获得了三项发明专利(专利号 ZLO 1100474.6、 ZL01100475.4及 ZL02156824.3 )0 在借鉴国内外提钾经验的基础上, 创造了一种水热化学反应法提钾新工艺, 可获得 KOH、 K2C03和 K2S04制品。其中采用的含钾硅酸盐岩石主要是由自生硅酸盐矿物所 组成的一类特殊岩石。 该类岩石中, 含钾矿物主要为钾长石、 伊利石、 海绿石、 云母 类矿物等, 化学成分中 K20含量较高, 一般在 10%以上。这些专利技术虽然可以将岩 石中原来不溶性钾转变成可溶于水中的钾, 但是同时也留下大量的固体残渣。 这些固 体残渣尚未找到合适的应用领域, 若长期堆放, 极易造成环境负担, 而且需要占用大 量土地。 . The inventors have also carried out research on extracting potassium from potassium-containing silicate rock (insoluble potassium ore) since 1996. Research, has won three invention patents (patent number ZLO 1100474.6, ZL01100475.4 and ZL02156824.3) 0 on the basis of learning from domestic and foreign experience in potassium, created a new hydrothermal chemical reaction method to extract potassium, KOH, K 2 C0 3 and K 2 S0 4 preparations were obtained. The potassium-containing silicate rock used is mainly a special type of rock composed of authigenic silicate minerals. In this type of rock, the potassium-bearing minerals are mainly potassium feldspar, illite, glauconite, mica minerals, etc. The chemical composition has a high K 2 0 content, generally more than 10%. Although these patented technologies can convert the original insoluble potassium in the rock into potassium which is soluble in water, it also leaves a large amount of solid residue. These solid residues have not yet found a suitable application area, and if they are stacked for a long time, they are highly liable to cause environmental burdens and require a large amount of land. .
综上可见, 在现有的水热化学反应法由含钾硅酸盐岩石制取钾肥的技术中, 通常 都是将岩石中的一种或几种元素转化为植物营养成分, 如钾肥、 磷肥、 钙镁肥、 硅钙 肥等。而且, 现有技术中使用的含钾硅酸盐岩石主要是由 κ2ο含量较高的自生硅酸盐 矿物组成的特殊岩石, 还没有一种利用普通的硅酸盐岩石生产矿物肥料的方法。 更重 要的是, 迄今为止, 还没有一种能够模拟地球化学风化成土过程、 将硅酸盐岩石中的 各种矿物质整体地转化成为植物生长的有效养分、 而且使其具有独特的微孔结构的技 术。 发明内容 In summary, in the existing hydrothermal chemical reaction method for preparing potassium fertilizer from potassium-containing silicate rock, one or several elements in the rock are usually converted into plant nutrients, such as potassium fertilizer and phosphate fertilizer. , calcium and magnesium fertilizer, silicon calcium fertilizer, etc. Moreover, the potassium-containing silicate rock used in the prior art is mainly a special rock composed of autogenous silicate minerals having a relatively high content of κ 2 ο, and there is no method for producing mineral fertilizer by using ordinary silicate rock. . More importantly, to date, there has not been an effective nutrient that can simulate the geochemical weathering process, transform the various minerals in silicate rock into plant growth, and make it unique. Structural technology. Summary of the invention
本发明的目的是: 提供一种能够将硅酸盐岩石中的主要元素和微量元素整体地转 化成能被植物吸收的多元素新型矿物肥料的水热化学反应方法。 SUMMARY OF THE INVENTION The object of the present invention is to provide a hydrothermal chemical reaction method capable of converting a main element and a trace element in a silicate rock into a multi-element novel mineral fertilizer which can be absorbed by a plant.
本发明解决其技术问题所釆用的方案之一是: 利用水热化学反应由硅酸盐岩石制 取多元素微孔矿物肥料, 其特点包括下列步骤: One of the solutions used by the present invention to solve its technical problems is: The use of hydrothermal chemical reaction to prepare multi-element microporous mineral fertilizer from silicate rock, the characteristics of which include the following steps:
( 1 ) 将硅酸盐岩石和碱土激发剂分别粉碎并磨细成粉状物料; (1) pulverizing and grinding the silicate rock and the alkaline earth activator into a powdery material;
(2) 按照 1:0.5〜1的硅酸盐岩石: 碱土激发剂比例, 将上述粉状物料投入水中, 使得水和粉状物料总重量的比例为 1〜3: 1 , 并进行搅拌混合; (2) according to 1:0.5~1 silicate rock: alkaline earth activator ratio, the above powdery material is put into water, so that the ratio of the total weight of water and powdery material is 1~3:1, and stirring and mixing;
(3) 将混合均匀的物料在封闭反应容器中于 1301〜 250Ό进行水热反应, 反应 时间为 5〜24小时; (3) hydrothermally reacting the uniformly mixed material in a closed reaction vessel at 1301 to 250 Torr for a reaction time of 5 to 24 hours;
(4) 将反应产物干燥、 粉碎过筛, 即可获得多元素微孔矿物肥料, (4) The reaction product is dried, pulverized and sieved to obtain a multi-element microporous mineral fertilizer.
其中所述的碱土激发剂包括石灰、 轻烧氧化镁和白云石灰。 The alkaline earth activators described therein include lime, light burned magnesia and dolomitic lime.
本发明解决其技术问题所采用的方案之二是: 利用水热化学反应由硅酸盐岩石制 取多元素微孔矿物肥料, 其特点包括下列步骤:
( 1 ) 将硅酸盐岩石、 碱土激发剂和活化剂分别粉碎并磨细成粉状物料; The second solution adopted by the present invention to solve the technical problem is: using a hydrothermal chemical reaction to prepare a multi-element microporous mineral fertilizer from a silicate rock, the characteristics of which include the following steps: (1) pulverizing and grinding the silicate rock, the alkaline earth activator and the activator into a powdery material;
(2) 按照硅酸盐岩石: 碱土激发剂: 活化剂之间 1:0.5〜1 :0.01〜0.25的比例, 将 上述粉状物料投入水中, 使得水和粉状物料总重量的比例为 1〜3: 1, 并进行搅拌混 (2) According to the ratio of silicate rock: alkaline earth activator: activator 1:0.5~1:0.01~0.25, the above powdery material is put into water so that the ratio of the total weight of water and powdery material is 1~ 3: 1, and mix and mix
Ώ; Ώ
(3 ) 将混合均匀的物料在封闭反应容器中于 13(rC〜25(TC进行水热反应, 反应 时间为 5〜24小时; (3) mixing the homogeneous material in a closed reaction vessel at 13 (rC~25 (TC hydrothermal reaction, reaction time is 5~24 hours;
(4) 将反应产物干燥、 粉碎过筛, 即可获得多元素微孔矿物肥料, (4) The reaction product is dried, pulverized and sieved to obtain a multi-element microporous mineral fertilizer.
其中所述的碱土激发剂包括石灰、 轻烧氧化镁和白云石灰, 并且所述的活化剂包 括石膏和硼酸镁。 The alkaline earth activator described therein includes lime, light burned magnesia and dolomitic lime, and the activator comprises gypsum and magnesium borate.
根据本发明所提供的方法由含钾硅酸盐岩石制备出的多元素微孔矿物肥料, 包含 Multi-element microporous mineral fertilizer prepared from a potassium-containing silicate rock according to the method provided by the present invention, comprising
15%〜30%的枸溶性硅、 30%〜40%的枸溶性钙镁、 4%〜6%的水溶性和枸溶性 K20、 1 %〜5%的枸溶性铁, 不含氯, 主要由托贝莫来石 [Ca5 Si6016(OH)2.4H20]和水合硅铝 酸钙 [Ca3Al2(Si04)(OH)8]两种合成矿物的显微晶体组成, 并且其中水合硅铝酸钙为 1-5 微米量级的球粒状, 托贝莫来石为数十〜数百纳米厚度的薄片状。 15%~30% 枸 soluble silicon, 30%~40% 枸 soluble calcium magnesium, 4%~6% water soluble and 枸 soluble K 2 0, 1%~5% 枸 soluble iron, chlorine free, Microscopy of two synthetic minerals mainly consisting of tobemorite [Ca 5 Si 6 0 16 (OH) 2 .4H 2 0] and hydrated calcium aluminosilicate [Ca 3 Al 2 (Si0 4 )(OH) 8 ] The crystal composition, and wherein the hydrated calcium aluminosilicate is granulated in the order of 1-5 micrometers, and the tobe mullite is flaky in the thickness of several tens to hundreds of nanometers.
本发明将硅酸盐岩石中的主要元素和微量元素整体地转化成能被植物吸收的多元 素矿物肥料, 革新了传统的单一元素化肥或简单几种元素复合肥料的概念。 而且本发 明的制备多元素矿物肥料的方法能够快速、 低成本地将硅酸盐岩石中的各种矿物质高 效且大比例地转化成为植物可以吸收的有效形态, 从而有可能从根本上结束人类有史 以来一直依赖于自然风化成土过程获得土壤有效矿物质养分的状态。 附图说明 The invention transforms the main elements and trace elements in the silicate rock into a multi-mineral mineral fertilizer which can be absorbed by the plant, and reforms the concept of the traditional single element fertilizer or the simple element compound fertilizer. Moreover, the method for preparing a multi-element mineral fertilizer of the present invention can rapidly and cost-effectively convert various minerals in a silicate rock into an effective form that the plant can absorb, thereby possibly ending the human being at the root. It has historically relied on the natural weathering process to obtain the state of effective mineral nutrients in the soil. DRAWINGS
图 1是水热反应产物的 X-射线粉晶衍射物相分析图; Figure 1 is an X-ray powder crystal diffraction phase analysis diagram of a hydrothermal reaction product;
图 2是水热反应产物的扫描电镜显微照片。 具体实施方式 Figure 2 is a scanning electron micrograph of a hydrothermal reaction product. detailed description
本发明中对用于生产矿物肥料的硅酸盐岩石没有任何特别限制, 并且无须进行选 矿、 焙烧等复杂的前期处理。 The silicate rock used for producing the mineral fertilizer is not particularly limited in the present invention, and complicated pre-treatment such as beneficiation, roasting, and the like is not required.
本发明中所釆用的碱土激发剂, 既可以是比较纯的工业石灰, 也可以是工业轻烧 氧化镁, 还可以用由白云石煅烧获得的白云石灰, 其中 CaO-MgO可为任意比例。 The alkaline earth activator used in the present invention may be either a relatively pure industrial lime or an industrial light burned magnesia, or a dolomitic lime obtained by calcination of dolomite, wherein CaO-MgO may be in any ratio.
本发明中所釆用的活化剂既可是石膏, 也可是硼酸镁。 在本发明中, 石膏的存在
大大激发了 Ca(OH)2或 /和 Mg(OH)2的活性, 使转化率更高。 而硼酸镁可以促进硅酸 盐矿物中硅氧四面体和铝氧四面体结构的崩解破坏, 从而达到提高转化率, 增加产品 中有效成分含量的目的。 The activator used in the present invention may be either gypsum or magnesium borate. In the present invention, the presence of gypsum The activity of Ca(OH) 2 or/and Mg(OH) 2 is greatly stimulated, resulting in higher conversion. Magnesium borate can promote the disintegration and destruction of the silicon oxytetrahedron and the aluminoxy tetrahedron structure in the silicate mineral, thereby achieving the purpose of increasing the conversion rate and increasing the content of the active ingredient in the product.
本发明中固体物料研磨的颗粒大小选择在 200目以下 (即 0.074mm以下)。 颗粒 过大影响反应速度, 致使产品中有效成分含量降低。 颗粒也不宜过细, 否则研磨中耗 电量增大, 导致生产成本上升。 In the present invention, the particle size of the solid material is selected to be less than 200 mesh (i.e., 0.074 mm or less). Excessive particle size affects the rate of reaction, resulting in a decrease in the amount of active ingredient in the product. The particles should not be too fine, otherwise the power consumption in the grinding will increase, resulting in an increase in production costs.
在本发明的制备方法中, 水的用量极其重要。 水量过少不能保证各种组分的溶出 效果, 而水量过多则使物料的处理量降低, 从而降低生产率。 本发明中水的用量是根 据固体物料的量进行选择的, 以使固体物料处于半湿状态。 在本发明中, 水和固体物 料的用量比, 即固液比, 为 1: 1〜3, 优选 1: 1.2〜1.5。 In the production method of the present invention, the amount of water is extremely important. Too little water does not guarantee the dissolution of the various components, while too much water reduces the throughput of the material, thereby reducing productivity. The amount of water used in the present invention is selected in accordance with the amount of the solid material so that the solid material is in a semi-wet state. In the present invention, the ratio of the amount of water to the solid material, i.e., the solid-liquid ratio, is 1:1 to 3, preferably 1:1.2 to 1.5.
另外, 反应体系中的压力对于水热反应也很重要。 在工业化生产中, 可以向反应 体系中通入蒸气以保持反应压力恒定。 一般而言, 压力越大, 越有利于水热反应的进 行。 但是, 考虑到设备成本和反应体系中已有的水的蒸发, 通入的蒸气的压力优选为 0.2〜5Mpa, 更优选为 0.5〜2Mpa, 最优选为约 1.2〜1.3Mpa。 In addition, the pressure in the reaction system is also important for the hydrothermal reaction. In industrial production, steam can be introduced into the reaction system to keep the reaction pressure constant. In general, the greater the pressure, the more favorable the hydrothermal reaction is. However, in view of equipment cost and evaporation of water already present in the reaction system, the pressure of the introduced vapor is preferably 0.2 to 5 MPa, more preferably 0.5 to 2 MPa, and most preferably about 1.2 to 1.3 MPa.
反应温度和时间是决定水热反应效果的重要因素。 一般而言, 较高的温度有利于 水热化学反应中含钾硅酸盐的结构崩解破坏, 从而达到提高转化率、 增加产品中有效 成分含量的目的, 同时也可以缩短反应时间, 提高生产率。 但过高的反应温度对反应 釜的耐热、 耐压性能要求更高、 更严, 导致设备投资加大, 不利于降低生产成本。 另 一方面, 较低的温度导致转化率下降, 产品中有效成分含量降低, 并且使反应时间过 长, 增加生产成本。 当温度低于 100°C, 即低于水的沸点时, 水热反应进行得极其缓 慢, 而且基本上得不到本发明的多元素微孔矿物肥料。 因此, 从获得理想的多元素矿 物肥料和降低成本考虑, 本发明的反应温度范围优选为 100〜300°C, 更优选 130〜 250°C, 最优选为 170〜200°C, 而反应时间优选为 5〜24小时, 更优选 7〜14小时。 The reaction temperature and time are important factors in determining the effect of the hydrothermal reaction. In general, the higher temperature facilitates the disintegration and destruction of the potassium-containing silicate in the hydrothermal chemical reaction, thereby achieving the purpose of increasing the conversion rate and increasing the content of the active ingredient in the product, and also shortening the reaction time and increasing the productivity. . However, the excessively high reaction temperature requires higher and stricter heat resistance and pressure resistance performance of the reactor, resulting in an increase in equipment investment, which is not conducive to reducing production costs. On the other hand, lower temperatures result in lower conversion rates, lower levels of active ingredients in the product, and excessive reaction times, increasing production costs. When the temperature is lower than 100 ° C, i.e., lower than the boiling point of water, the hydrothermal reaction proceeds extremely slowly, and the multi-element microporous mineral fertilizer of the present invention is substantially not obtained. Therefore, the reaction temperature range of the present invention is preferably from 100 to 300 ° C, more preferably from 130 to 250 ° C, most preferably from 170 to 200 ° C, from the viewpoint of obtaining an ideal multi-element mineral fertilizer and reducing cost, and the reaction time is preferably It is 5 to 24 hours, more preferably 7 to 14 hours.
本发明的水热反应在静态条件下进行, 既可大大降低能源消耗, 又使技术简单, 工艺流程上易于实现, 且工人易于操作实施。 而且整个生产过程中无废水、 废气和固 体废物的排放, 属于绿色环保型工艺技术。 The hydrothermal reaction of the present invention is carried out under static conditions, which can greatly reduce energy consumption, make the technology simple, and is easy to implement in the process flow, and the worker is easy to operate and implement. Moreover, there is no discharge of waste water, waste gas and solid waste in the whole production process, which is a green environmental protection technology.
对热水反应产物按照农业部规定的程序开展溶解试验的结果表明, 其固相物质组 成的 65%-95%都能够溶解于 0.5摩尔的盐酸溶液之中, 属于能够被植物所吸收的水溶 性或枸溶性组分。 其中水溶性和枸溶性 K20的含量约为 4%-6% (相当于目前市场上 出售的钾钙肥), 是一种无氯钾肥。 同时还含 20%±的枸溶性硅(达到了农业部颁布的
硅肥标准)、 ≥30%的枸溶性钙镁、 1%-5%的枸溶性铁以及较大比例的其它枸溶性组分 (包括硅酸盐岩石中的各种微量元素和稀土元素)。 因此本产品是一种良好的钾、 硅、 钙、 镁、 铁、 锰、 硼等多元素长效缓释矿物肥料。 The results of the dissolution test on the hot water reaction product according to the procedures prescribed by the Ministry of Agriculture indicate that 65%-95% of the solid phase material composition can be dissolved in 0.5 mole hydrochloric acid solution, which is a water-soluble substance that can be absorbed by plants. Or hydrazine soluble components. The water-soluble and hydrazine-soluble K 2 0 content is about 4%-6% (equivalent to the potassium and calcium fertilizer currently on the market), and is a chlorine-free potassium fertilizer. It also contains 20% ± 枸 soluble silicon (achieved by the Ministry of Agriculture Silicon fertilizer standard), ≥30% bismuth-soluble calcium and magnesium, 1%-5% bismuth-soluble iron and a large proportion of other bismuth-soluble components (including various trace elements and rare earth elements in silicate rock). Therefore, this product is a good long-acting slow-release mineral fertilizer with potassium, silicon, calcium, magnesium, iron, manganese and boron.
由图 1显示的热水反应产物的 X-射线粉晶衍射物相分析结果可见,本发明的多元 素矿物肥料主要由 以下两种合成矿物的微细晶体组成: 托贝莫来石 [Ca5Si6016(OH)2.4¾0]和水合硅铝酸钙 [Ca3Al2(Si04)(OH) From the results of X-ray powder crystal diffraction phase analysis of the hot water reaction product shown in Fig. 1, it can be seen that the multi-element mineral fertilizer of the present invention is mainly composed of fine crystals of the following two synthetic minerals: Tobe mullite [Ca 5 Si 6 0 16 (OH) 2 .43⁄40] and hydrated calcium aluminosilicate [Ca 3 Al 2 (Si0 4 )(OH)
图 2显示了本发明的多元素矿物肥料的扫描电子显微镜分析结果。 根据颗粒形态 '大小的观察以及显微结构的分析, 组成本新型矿物肥料的颗粒非常微细, 为纳米 -亚微 米级; 其中水合硅铝酸钙为微米级的球粒状(粒径 1-5微米), 托贝莫来石则呈纳米级 的薄片状 (薄片的厚度为数十-数百个纳米)。 而且, 本矿物肥料在扫描电子显微镜下 还显示极为发达的微孔结构, 故本矿物肥料质地疏松, 容重只有 0.70-0.80g/cm3, 因此 也称其为微孔矿物肥料。 由于本矿物肥料独特的微细颗粒和微孔结构, 其具有非常髙 的活性, 大大提高了其被植物根酸溶解吸收的能力。 而且, 本产品特有的微孔结构还 使其具有保水保肥、 改良土壤团粒结构、 促进植物根部通风透气的功能。 Figure 2 shows the results of scanning electron microscopy analysis of the multi-element mineral fertilizer of the present invention. According to the observation of the particle size' size and the analysis of the microstructure, the particles of the new type of mineral fertilizer are very fine, and are nano-submicron; wherein the hydrated calcium aluminosilicate is micron-sized granules (particle size 1-5 microns). ), the tobemorite stone is in the form of nano-scale flakes (the thickness of the flakes is tens to hundreds of nanometers). Moreover, the mineral fertilizer also shows a highly developed microporous structure under a scanning electron microscope, so the mineral fertilizer has a loose texture and a bulk density of only 0.70-0.80 g/cm 3 , so it is also called a microporous mineral fertilizer. Due to the unique fine particles and microporous structure of the mineral fertilizer, it has very high activity, which greatly improves its ability to be dissolved and absorbed by the plant root acid. Moreover, the unique microporous structure of this product also has the functions of retaining water and ensuring fertilizer, improving soil aggregate structure, and promoting ventilation and ventilation of plant roots.
本矿物肥料独特的微细颗粒和微孔结构是因为在其制备过程中釆用了独有的碱土 激发剂的应用和半湿状态的工艺, 而且恰到好处地控制了水热化学反应的温度、 压力 和时间。 而使用焙烧工艺生产的钾硅钙肥、 使用磷化工厂的黄磷渣和钢铁企业的钢渣 生产的硅钙肥, 在扫描电子显微镜下都不具备这种微孔结构, 并且 X-射线粉晶衍射物 相分析显示其为非晶态或隐晶质结构。 The unique fine-grained and microporous structure of this mineral fertilizer is due to the use of a unique alkaline earth activator and a semi-wet process during its preparation, and the temperature, pressure and hydrothermal reaction are controlled just right. time. The potassium silicon calcium fertilizer produced by the roasting process, the yellow phosphorus slag produced by the phosphating plant, and the silicon calcium fertilizer produced by the steel slag of the steel enterprise do not have such a microporous structure under the scanning electron microscope, and the X-ray powder crystal Diffraction phase analysis shows that it is amorphous or cryptocrystalline.
本发明的多元素微孔矿物肥料没有加入任何有害物质, 保留了硅酸盐岩石自身的 天然物质成分特征, 与天然风化形成的土壤一样, 农田施用后不会产生格外的毒害和 污染, 适合于生产天然绿色食品。 并且本发明的多元素微孔矿物肥料产品作为枸溶性 长效缓释肥, 不会引起农业面源污染。 The multi-element microporous mineral fertilizer of the invention does not contain any harmful substances, and retains the natural material composition characteristics of the silicate rock itself. Like the soil formed by natural weathering, the farmland does not cause extratoxicity and pollution after application, and is suitable for Produce natural green food. Moreover, the multi-element microporous mineral fertilizer product of the invention can not cause agricultural non-point source pollution as a long-acting slow-release fertilizer.
2006年和 2007年在北京、 河北、 吉林、 内蒙、 四川、 贵州、 福建、 江西、 新疆、 山东、 辽宁等地对玉米、 水稻、 小麦、 糯玉米、 苹果、 水蜜祧、 葡萄、 冬枣、 茶叶、 向日葵、 辣椒、 白菜、 油菜、 芹菜、 蚕豆、 地瓜等农作物开展了初步田间肥效试验, 取得了较好的效果。 各种农产品的产量增加可分别达到 2%-20% (参见附件 1 )。 据农 业部谷物品质监督检验测试中心检测, 水稻的品质也有所提高, 与不施本矿物肥料的 水稻相比较, 其检测的十项品质指标 (水分、 粗蛋白、 直链淀粉、 糙米率、 糯米率、 整 糯米率、 胶稠度、 碱消值 (级) /糊化温度、 垩白米率、 垩白大小、 坚白度) 中的九项 (垩
白米率除外)均有不同程度的提高 (参见附件 2)。 下面结合具体的实施例更详细地描述本发明, 但是这些实施例仅用于说明目的, 而不以任何方式限制本发明的范围。 实施例 1 In 2006 and 2007, in Beijing, Hebei, Jilin, Inner Mongolia, Sichuan, Guizhou, Fujian, Jiangxi, Xinjiang, Shandong, Liaoning and other places on corn, rice, wheat, waxy corn, apples, candied fruit, grapes, winter jujube, tea, Sunflower, pepper, cabbage, rapeseed, celery, broad beans, sweet potatoes and other crops carried out preliminary field fertilizer efficiency tests, and achieved good results. The increase in production of various agricultural products can reach 2%-20% respectively (see Annex 1). According to the inspection of the Grain Quality Supervision and Inspection Center of the Ministry of Agriculture, the quality of rice has also improved. Compared with rice without mineral fertilizer, the ten quality indicators (moisture, crude protein, amylose, brown rice rate, glutinous rice) are detected. Nine items in rate, whole rice rate, gel consistency, alkali value (grade) / gelatinization temperature, chalky rice rate, chalk size, whiteness (垩) The white rice rate has a different degree of improvement (see Annex 2). The invention is described in more detail below with reference to the specific embodiments thereof, but these examples are intended to be illustrative only and not to limit the scope of the invention in any way. Example 1
1 ) 选取原料, 包括含钾岩石和石灰: 1) Select raw materials, including potassium-containing rocks and limes:
含钾硅酸盐岩石: 釆自北京市密云县南山, 它的化学组成 (%) 如下
Potassium-containing silicate rock: from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows
X射线粉晶衍射分析指出, 该含钾岩石以钾长石为主, 其它为石英等。 X-ray powder crystal diffraction analysis indicates that the potassium-containing rock is mainly potassium feldspar, and the other is quartz.
石灰: 含 CaO 97% (化学纯, 中国医药公司北京釆购供应站)。 Lime: Contains 97% of CaO (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
2) 生产过程: 2) Production process:
( 1 ) 将含钾岩石、 石灰分别粉碎至 200目以下, 先在塑料器皿内加入 30ml水, 然后依次往皿内加入 5.000克含钾岩石矿粉、 5.000克石灰粉, 用搅拌棒搅拌均匀; (1) pulverize the potassium-containing rock and lime to below 200 mesh, first add 30 ml of water to the plastic vessel, then add 5.000 g of potassium-containing rock ore powder and 5.000 g of lime powder to the vessel in turn, and stir evenly with a stir bar;
(2) 将盛有样品的塑料器皿置入高压反应釜中, 在 197Ό反应 7小时; (2) The plastic vessel containing the sample is placed in an autoclave and reacted at 197 Torr for 7 hours;
(3 )高压反应釜冷却后取出塑料器皿, 将反应产物转移至玻璃表皿上, 在 105Ό 烘箱内加热烘干, 磨细, 即获得矿物肥料产品。 (3) After the high pressure reactor is cooled, the plastic vessel is taken out, the reaction product is transferred to a glass watch, heated and dried in a 105 烘 oven, and ground to obtain a mineral fertilizer product.
3 )为了测定含钾矿物中钾的溶出率, 将获得的产品移入过滤器, 用水浸取出可溶 性钾。 试验中获得 100ml含钾过滤液, 稀释后用火焰光度计测得液样中钾的浓度, 测 定结果换算成 K20浓度为 4540ing/l。 5.000克含钾岩石矿粉含 K20 639.5mg, 而浸取 液折合 K20浓度为 4540mg/l, 贝 Ij lOO ml过滤液含有 K20 454.0mg, 因此, 含钾矿物 中钾的溶出率为 70.99%。 实施例 2 3) In order to determine the dissolution rate of potassium in the potassium-containing mineral, the obtained product is transferred to a filter, and the soluble potassium is extracted by water. In the test, 100 ml of potassium-containing filtrate was obtained, and after dilution, the concentration of potassium in the liquid sample was measured by a flame photometer, and the measurement result was converted into a K 2 0 concentration of 4540 ng/l. 5.000 g of potassium-containing rock ore powder contains K 2 0 639.5 mg, and the leachate is equivalent to K 2 0 concentration of 4540 mg/l, and the shell Ij lOO ml filtrate contains K 2 0 454.0 mg, therefore, dissolution of potassium in potassium-containing minerals The rate was 70.99%. Example 2
1 ) 选取原料, 包括含钾岩石、 石灰和石膏: 1) Select raw materials, including potassium-containing rock, lime and gypsum:
含钾硅酸盐岩石: 釆自北京市密云县南山, 它的化学组成 (%) 如下
Potassium-containing silicate rock: from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows
X射线粉晶衍射分析指出, 该含钾岩石以钾长石为主, 其它为石英等。
石灰: 含 Ca0 97% (化学纯, 购自中国医药公司北京供应站)。 X-ray powder crystal diffraction analysis indicates that the potassium-containing rock is mainly potassium feldspar, and the other is quartz. Lime: Contains 97% of Ca0 (chemically pure, purchased from China Pharmaceuticals Beijing Supply Station).
石膏: 釆自新疆和布克赛尔县夏子盖膨润土矿区, 为结晶完好的透明石膏, 实验 室烘箱内 120Ό加热 1小时, 获得半水石膏 (CaS04 · 1/2H20)。 Gypsum: From the Xinjiang and Buxail County Xiazizi bentonite mining area, for the crystallized transparent gypsum, heated in a laboratory oven for 120 hours to obtain hemihydrate gypsum (CaS0 4 · 1/2H 2 0).
2) 生产过程: 2) Production process:
( 1 )将含钾岩石、石灰、 半水石膏分别粉碎至 200目以下, 先在塑料器皿内加入 (1) crush the potassium-containing rock, lime and hemihydrate gypsum to below 200 mesh, first in the plastic vessel
30ml水, 然后依次往皿内加入 1.000克半水石膏粉、 5.000克含钾岩石矿粉、 4.000克 石灰粉, 用搅拌棒搅拌均匀; 30ml of water, then add 1.000g of hemihydrate gypsum powder, 5.000g of potassium-containing rock ore powder, 4.000g of lime powder to the dish, and stir evenly with a stir bar;
(2) 将盛有样品的塑料器皿置入高压反应釜中, 在 197Ό反应 7小时; (2) The plastic vessel containing the sample is placed in an autoclave and reacted at 197 Torr for 7 hours;
(3 )高压反应釜冷却后取出塑料器皿, 将反应产物转移至玻璃表皿上, 在 105°C 烘箱内加热烘干, 磨细, 即获得矿物肥料产品。 (3) After the high pressure reactor is cooled, the plastic vessel is taken out, the reaction product is transferred to a glass watch, heated and dried in an oven at 105 ° C, and finely ground to obtain a mineral fertilizer product.
3)为了测定含钾矿物中钾的溶出率, 将获得的产品移入过滤器, 用水浸取出可溶 性钾。 试验中获得 100ml含钾过滤液, 稀释后用火焰光度计测得液样中钾的浓度, 测 定结果换算成 K20浓度为 5080mg/L 5.000克含钾岩石矿粉含 K20 639.5mg, 而浸取 液折合 K20浓度为 5080mg/l, 则 100 ml过滤液含有 K20 508.0mg, 因此, 含钾矿物 中钾的溶出率为 79.44%。 比较实施例 1和例 2, 可以看出配方中加入一定量的石膏 (本处为半水石膏), 激 发了石灰的活性, 使含钾岩石中钾的溶出率提高了 8.45%。 实施例 3 3) In order to determine the dissolution rate of potassium in the potassium-containing mineral, the obtained product was transferred to a filter, and the soluble potassium was extracted with water. In the test, 100 ml of potassium-containing filter solution was obtained. After dilution, the concentration of potassium in the liquid sample was measured by a flame photometer. The measurement result was converted into a K 2 0 concentration of 5080 mg/L 5.000 g of potassium-containing rock ore powder containing K 2 0 639.5 mg. When the leachate is equivalent to a K 20 concentration of 5080 mg/l, 100 ml of the filtrate contains K 2 0 508.0 mg, and therefore, the dissolution rate of potassium in the potassium-containing mineral is 79.44%. Comparing Example 1 and Example 2, it can be seen that a certain amount of gypsum (herely hemihydrate gypsum) was added to the formulation, which stimulated the activity of lime, and the dissolution rate of potassium in the potassium-containing rock was increased by 8.45%. Example 3
1 ) 选取原料, 包括含钾岩石和石灰: 1) Select raw materials, including potassium-containing rocks and limes:
含钾硅酸盐岩石: 采自北京市密云县南山, 它的化学组成 (%) 如下:
Potassium-containing silicate rock: taken from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows:
X射线粉晶衍射分析指出, 该硅酸盐岩石矿物组成以钾长石为主,其它为石英等。 石灰: 含 CaO 97% (化学纯, 中国医药公司北京釆购供应站)。 X-ray powder crystal diffraction analysis indicates that the silicate rock mineral composition is mainly potassium feldspar, and the others are quartz. Lime: Contains 97% of CaO (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
2) 生产过程: 2) Production process:
( 1 ) 将硅酸盐岩石、 石灰分别磨细至 200目以下, 得到硅酸盐岩石粉, 石灰粉; 在塑料器皿内加入 15ml水, 然后将 5.700g硅酸盐岩石粉、 4.300g石灰粉依次加入到 器皿中, 并进行搅拌, 使物料混合均匀;
(2) 将盛有样品的塑料器皿置入高压反应釜中, 在 191 °C反应 8小时;(1) The silicate rock and lime are respectively ground to below 200 mesh to obtain silicate rock powder and lime powder; 15 ml of water is added to the plastic vessel, and then 5.700 g of silicate rock powder and 4.300 g of lime powder are added. Add to the vessel in turn, and stir to mix the materials evenly; (2) The plastic vessel containing the sample is placed in an autoclave and reacted at 191 ° C for 8 hours;
(3)高压反应釜冷却后,取出塑料器皿,将反应产物转移至玻璃表皿中,在 105Ό 烘箱内加热烘干; (3) After the autoclave is cooled, the plastic vessel is taken out, and the reaction product is transferred to a glass watch and heated and dried in a 105 烘 oven;
(4) 将干燥后的反应产物磨细, 即获得多元素矿物肥料。 (4) The dried reaction product is ground to obtain a multi-element mineral fertilizer.
3 ) 测量获得的多元素矿物肥料的有效成分含量 (l.OOOg 多元素矿物肥料样品在 3) Measure the active ingredient content of the multi-element mineral fertilizer obtained (l.OOOg multi-element mineral fertilizer sample at
100ml 0.5mol/l盐酸中的溶出量, 室温, 溶解时间为 30分钟, 电磁搅拌), 结果如表 1 所示。 表 1 实施例 3多元素矿物肥料有效成分含量 (%)
The elution amount in 100 ml of 0.5 mol/l hydrochloric acid, room temperature, dissolution time was 30 minutes, electromagnetic stirring), and the results are shown in Table 1. Table 1 Example 3 Multi-element mineral fertilizer active ingredient content (%)
所用仪器: 全谱直读等离子发射光谱仪, IRIS Advantage型, 美国热电公司生产 实施例 4 Instrument used: Full spectrum direct reading plasma emission spectrometer, IRIS Advantage type, American Thermoelectric Company production Example 4
1 ) 选取原料, 包括含钾硅酸盐岩石、 石灰和轻烧硼镁石矿: 1) Select raw materials, including potassium silicate rock, lime and light burned boehmite:
含钾硅酸盐岩石: 釆自北京市密云县南山, 它的化学组成 (%) 如下; Potassium-containing silicate rock: from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows;
X射线粉晶衍射分析指出, 该含钾岩石矿物组成以钾长石为主, 其它为石英等。 石灰: CaO含量 97%, (化学纯, 中国医药公司北京釆购供应站)。 X-ray powder crystal diffraction analysis indicated that the potassium-bearing rock mineral composition is mainly potassium feldspar, and the others are quartz. Lime: CaO content 97%, (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
轻烧硼镁石矿:原矿样获自辽宁天承化工厂,将原矿粗碎样置于马弗炉内,在 70(TC 加热恒温 0.5小时, 取出, 获得物相以玻璃态为主的轻烧硼镁石矿。 Light burned boehmite ore: The original ore sample was obtained from Liaoning Tiancheng Chemical Plant, and the raw ore coarse crushed sample was placed in a muffle furnace. At 70 (TC heating and constant temperature for 0.5 hour, it was taken out to obtain a light phase dominated by the glass phase. Burning magnesia ore.
2) 生产过程- ( 1 )将含钾岩石、 石灰、 轻烧硼镁石矿分别粉碎至 200目以下, 先在塑料器皿内 加入 15ml水, 然后依次往皿内加入 lOOmg轻烧硼镁石矿粉、 5.700g含钾岩石矿粉、 4,200g石灰粉, 用搅拌棒搅拌均匀。 2) Production process - (1) Smash the potassium-bearing rock, lime, and light-burned borax ore to below 200 mesh, first add 15 ml of water to the plastic vessel, and then add 100 mg of light burnt magnesia ore to the vessel. Powder, 5.700g of potassium-containing rock ore powder, 4,200g of lime powder, stir well with a stir bar.
(2) 将盛有样品的塑料器皿置于高压反应釜中, 在 19CTC反应 8小时; (2) placing the plastic vessel containing the sample in an autoclave and reacting at 19 CTC for 8 hours;
(3) 高压反应釜冷却后取出塑料器皿, 将反应产物移至玻璃表面皿上, 在 105°C 烘箱内加热烘干;
(4) 将干燥后的反应产物磨细, 即获得多元素微孔矿物肥料。 (3) After the autoclave is cooled, the plastic vessel is taken out, the reaction product is transferred to a glass watch glass, and dried in an oven at 105 ° C; (4) The dried reaction product is ground to obtain a multi-element microporous mineral fertilizer.
3 ) 测量获得的多元素矿物肥料的有效成分含量 (l.OOOg矿物肥料样品在 100ml 0.5mol/l盐酸中的溶出量, 室温, 溶解时间为 30分钟, 电磁搅拌), 结果如表 2所示。 表 2 实施例 4多元素微孔矿物肥料有效成分含量 (%)
3) Measure the active ingredient content of the multi-element mineral fertilizer obtained (the dissolution amount of the 1000g mineral fertilizer sample in 100ml 0.5mol/l hydrochloric acid, room temperature, dissolution time 30 minutes, electromagnetic stirring), the results are shown in Table 2. . Table 2 Example 4 Multi-element microporous mineral fertilizer active ingredient content (%)
所用仪器: 全谱直读等离子发射光谱仪, IRIS Advantage型, 美国热电公司生产 对比实施例 3和例 4, 可以发现, 由于配方中加入了适量的轻烧硼镁石矿粉, 进 一步激发了石灰的活性, 可以促进硅酸盐矿物中硅氧四面体和铝氧四面体结构的崩解 破坏, 从而达到提高转化率, 增加产品中有效成分含量的目的。 实施例 5 Apparatus used: Full-spectrum direct-reading plasma emission spectrometer, IRIS Advantage type, American Thermoelectric Company produced Comparative Examples 3 and 4, it can be found that lime was added to the formula by adding an appropriate amount of light burnt magnesia ore fines. The activity can promote the disintegration and destruction of the silicon oxytetrahedron and the aluminoxy tetrahedral structure in the silicate mineral, thereby achieving the purpose of increasing the conversion rate and increasing the content of the active ingredient in the product. Example 5
1 ) 选取原料, 包括含钾硅酸盐岩石和石灰: 1) Select raw materials, including potassium silicate rock and lime:
含钾硅酸盐岩石: 采自北京市密云县南山, 它的化学组成 (%) 如下:
Potassium-containing silicate rock: taken from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows:
X射线粉晶衍射分析指出, 该含钾岩石矿物组成以钾长石为主, 其它为石英等。 石灰: CaO含量 97%, (化学纯, 中国医药公司北京釆购供应站)。 X-ray powder crystal diffraction analysis indicated that the potassium-bearing rock mineral composition is mainly potassium feldspar, and the others are quartz. Lime: CaO content 97%, (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
2) 生产过程: 2) Production process:
( 1 ) 将含钾岩石和石灰分别粉碎至 200目, 先在塑料器皿内加入 15ml 7 , 然后 依次往皿内加入 5.700g含钾岩石矿粉、 4.300g石灰粉, 用搅拌棒搅拌均匀。 (1) Smash the potassium-containing rock and lime to 200 mesh, first add 15ml 7 to the plastic vessel, then add 5.700g of potassium-containing rock ore powder and 4.300g of lime powder to the vessel, and stir evenly with a stir bar.
(2) 将盛有样品的塑料器皿置于高压反应釜中, 在 130'C反应 24小时; (2) placing the plastic vessel containing the sample in an autoclave and reacting at 130 ° C for 24 hours;
(3 ) 高压反应釜冷却后取出塑料器皿, 将反应产物移至玻璃表面皿上, 在 105°C 烘箱内加热烘干; (3) After the autoclave is cooled, the plastic vessel is taken out, and the reaction product is transferred to a glass watch glass, and dried in an oven at 105 ° C;
(4) 将干燥后的反应产物磨细, 即获得多元素微孔矿物肥料。 (4) The dried reaction product is ground to obtain a multi-element microporous mineral fertilizer.
3 ) 测量获得的多元素矿物肥料的有效成分含量 (l .OOOg矿物肥料样品在 100ml 0.5mol/l盐酸中的溶出量, 室温, 溶解时间为 30分钟, 电磁搅拌), 结果如表 3所示。
表 3 实施例 5多元素微孔矿物肥料有效成分含量 (%)
3) Measure the active ingredient content of the multi-element mineral fertilizer obtained (the dissolution amount of 1.000g mineral fertilizer sample in 100ml 0.5mol/l hydrochloric acid, room temperature, dissolution time is 30 minutes, electromagnetic stirring), the results are shown in Table 3. . Table 3 Example 5 multi-element microporous mineral fertilizer active ingredient content (%)
所用仪器: 全谱直读等离子发射光谱仪, IRIS Advantage型, 美国热电公司生产 实施例 6 Instrument used: Full spectrum direct reading plasma emission spectrometer, IRIS Advantage type, American Thermoelectric Company production Example 6
1 ) 选取原料, 包括含钾硅酸盐岩石和石灰: 1) Select raw materials, including potassium silicate rock and lime:
含钾硅酸盐岩石: 采自北京市密云县南山, 它的化学组成 (%〉 如下:
Potassium-containing silicate rock: taken from Nanshan, Miyun County, Beijing, its chemical composition (%> is as follows:
X射线粉晶衍射分析指出, 该含钾岩石矿物组成以钾长石为主, 其它为石英等。 石灰: CaO含量 97%, (化学纯, 中国医药公司北京釆购供应站)。 X-ray powder crystal diffraction analysis indicated that the potassium-bearing rock mineral composition is mainly potassium feldspar, and the others are quartz. Lime: CaO content 97%, (chemically pure, China Pharmaceuticals Beijing Purchasing and Supply Station).
2) 生产过程: 2) Production process:
( 1 ) 将含钾岩石和石灰分别粉碎至 200目, 先在塑料器皿内加入 15ml水, 然后 依次往皿内加入 5.700g含钾岩石矿粉、 4.300g石灰粉, 用搅拌棒搅拌均匀。 (1) Smash the potassium-containing rock and lime to 200 mesh, first add 15 ml of water to the plastic vessel, then add 5.700 g of potassium-containing rock ore powder and 4.300 g of lime powder to the vessel in turn, and stir well with a stir bar.
(2) 将盛有样品的塑料器皿置于高压反应釜中, 在 250Ό反应 5小时; (2) placing the plastic vessel containing the sample in an autoclave and reacting at 250 Torr for 5 hours;
(3 ) 高压反应釜冷却后取出塑料器皿, 将反应产物移至玻璃表面皿上, 在 105Ό 洪箱内加热烘干; (3) After the autoclave is cooled, the plastic vessel is taken out, and the reaction product is transferred to a glass watch glass and heated and dried in a 105-inch water tank;
(4) 将干燥后的反应产物磨细, 即获得多元素微孔矿物肥料。 (4) The dried reaction product is ground to obtain a multi-element microporous mineral fertilizer.
3 ) 测量获得的多元素矿物肥料的有效成分含量 (l.OOOg矿物肥料样品在 100ml 0.5mol/l盐酸中的溶出量, 室温, 溶解时间为 30分钟, 电磁搅拌), 结果如表 4所示。 表 4 实施例 6多元素微孔矿物肥料有效成分含量 (%)
3) Measure the active ingredient content of the multi-element mineral fertilizer obtained (the dissolution amount of the 1000g mineral fertilizer sample in 100ml 0.5mol/l hydrochloric acid, room temperature, dissolution time 30 minutes, electromagnetic stirring), the results are shown in Table 4. . Table 4 Example 6 multi-element microporous mineral fertilizer active ingredient content (%)
所用仪器: 全谱直读等离子发射光谱仪, IRIS Advantage型, 美国热电公司生产 对比实施例 5和例 6可以发现, 高温有利于水热化学反应中含钾硅酸盐的结构崩 解破坏, 从而达到提高转化率、 增加产品中有效成分含量的目的。
实施例 7 Instruments used: Full spectrum direct reading plasma emission spectrometer, IRIS Advantage type, American Thermoelectric Company production comparison Examples 5 and 6 can be found that high temperature is beneficial to the disintegration and destruction of potassium silicate containing structure in hydrothermal chemical reaction. Improve the conversion rate and increase the content of active ingredients in the product. Example 7
(1)选取原料, 包括: (1) Select raw materials, including:
富钾岩石: 采自北京市密云县南山, 它的化学组成 (%) 如下:
Potassium-rich rock: taken from Nanshan, Miyun County, Beijing, its chemical composition (%) is as follows:
X射线粉晶衍射分析指出, 该富钾岩石矿物组成以钾长石为主, 其它为石英等。 X-ray powder diffraction analysis indicates that the potassium-rich rock mineral composition is mainly potassium feldspar, and the others are quartz.
白云石灰: 含 CaO 53.23 %、 MgO 36.27%、 烧失量 8.07% , 取自河北省怀来县八 宝山石灰石矿。 Baiyun Lime: Containing 53.23 % of CaO, 36.27% of MgO, and 8.07% loss on ignition, taken from the Babaoshan limestone mine in Huailai County, Hebei Province.
半水石膏: 购于市场。 Semi-hydrated gypsum: purchased from the market.
(2) 将富钾岩石粗粉 5.000g, 石灰粗粉 5.000g, 半水石膏 l.OOOg置入研磨机中 充分研磨, 使上述物料粒度达到 200目以下, 并均匀混合, 在塑料器皿内加入 16.5ml 水, 然后将物料转移至塑料器皿内, 用玻棒搅拌均匀; (2) Put the potassium-rich rock coarse powder 5.000g, the lime coarse powder 5.000g, the hemihydrate gypsum l.OOg into the grinder and grind it thoroughly, so that the above-mentioned material has a particle size of less than 200 mesh, and uniformly mix and add in the plastic vessel. 16.5ml of water, then transfer the material to a plastic container and mix well with a glass rod;
(3 ) 将盛有样品的塑料器皿置入髙压反应釜中, 在 193°C恒温 8小时; (3) The plastic vessel containing the sample is placed in a pressure reactor and kept at a constant temperature of 193 ° C for 8 hours;
(4)高压反应釜冷却后取出塑料器皿, 将反应产物移入过滤器, 进行过滤, 试验 中获得 101ml含钾提取液; (4) After the autoclave is cooled, the plastic vessel is taken out, the reaction product is transferred to a filter, and filtered, and 101 ml of a potassium-containing extract is obtained in the test;
( 5 ) 将提取液稀释 20x10 = 200 倍 (两级稀释), 用火焰光度计测定 试样中的钾、钠浓度,测定结果换算成 K20及 Na20浓度分别为 6400mg/l及 260mg/l, 其 Na20/K20浓度比为 0.0406; (5) Dilute the extract by 20x10 = 200 times (two-stage dilution), determine the potassium and sodium concentrations in the sample by flame photometer, and convert the results into K 2 0 and Na 2 0 concentrations of 6400 mg/l and 260 mg, respectively. /l, the Na 2 0 / K 2 0 concentration ratio is 0.0406;
(6) 5. 000克富钾岩石矿粉含 K20 674.0mg, 提取液折合 K20浓度 6400mg/l, 则 101ml含有 K20 646.4mg,因此,富钾岩石中钾的转化提取率为(646.4÷674.0) xlOO % =95.91 %。 (6) 5. 000 g of potassium-rich rock ore powder contains K 2 0 674.0 mg, and the extract is equivalent to K 2 0 concentration of 6400 mg/l, then 101 ml contains K 2 0 646.4 mg, therefore, the conversion yield of potassium in potassium-rich rock (646.4÷674.0) xlOO % =95.91 %.
从实施例 7可以看出, 原料中的不可溶钾转化成为可溶性钾的最大转化率可以达 到 95.91%。 As can be seen from Example 7, the maximum conversion rate of the insoluble potassium in the raw material to soluble potassium can reach 95.91%.
实施例 8: (5吨级工业性制备试验) Example 8: (5-ton industrial preparation test)
1 ) 选取原料, 包括含钾硅酸盐岩石、 石灰和石膏: 1) Select raw materials, including potassium silicate rock, lime and gypsum:
含钾硅酸盐岩石: 釆自河北省张家口市宣化, 其化学组成 (%) 如下:
Potassium-containing silicate rock: 宣 from Xuanhua, Zhangjiakou City, Hebei Province, its chemical composition (%) is as follows:
X射线粉晶衍射分析指出, 其矿物组成以钾长石和伊利石为主, 其它为石英等。 石灰: 含 CaO 84%, 含 Mg0 3%, 宣化钢铁公司龙阳钙灰厂生产。
石膏: 二水石膏, 购自宣化建材商店。 X-ray powder diffraction analysis indicates that the mineral composition is mainly potassium feldspar and illite, and the others are quartz. Lime: Containing 84% CaO, containing Mg0 3%, produced by Xuanhua Iron and Steel Company Longyang Calcium Plant. Gypsum: Dihydrate gypsum, purchased from Xuanhua Building Materials Store.
2) 制备过程: 2) Preparation process:
( 1 )将含钾硅酸盐岩石、 石灰、 石膏分别磨细至 200目以下, 得到含钾硅酸盐岩 石粉、 石灰粉和石膏矿粉; 三种原料按下表比例配比- 表 5 实施例 Ί多元素微孔矿物肥料的原料配比
(1) The potassium silicate rock, lime and gypsum are respectively ground to below 200 mesh to obtain potassium silicate rock powder, lime powder and gypsum mineral powder; the three raw materials are proportioned according to the following table - Table 5 Example 原料 Raw material ratio of multi-element microporous mineral fertilizer
(2) 首先在贮料罐中放入 1270L 自来水, 然后将 lOOKg石膏粉、 500Kg含钾硅 酸盐岩石粉、 400Kg石灰粉依次加入到水中, 并进行搅拌, 使物料混合均勾, 共配制 5吨物料 (即配制 5罐物料)。 (2) First put 1270L tap water in the storage tank, then add lOOKg gypsum powder, 500Kg potassium silicate rock powder, 400Kg lime powder to the water in turn, and stir to mix the materials, and prepare 5 Tons of material (ie, 5 cans of material).
(3 ) 将物料转移至高压反应釜中, 通入高压蒸气 (0.95〜1.05MPa), 在 183Ό反应 10小时。 (3) The material was transferred to a high pressure reactor, and subjected to high pressure steam (0.95 to 1.05 MPa), and reacted at 183 Torr for 10 hours.
(4) 水热化学反应完成后降压降温, 打幵反应釜, 取出反应产物, 自然风干, 粉 碎后即得多元素微孔矿物肥料。 (4) After the completion of the hydrothermal chemical reaction, the pressure is lowered and the temperature is lowered. The reaction kettle is smashed, the reaction product is taken out, and it is naturally air-dried. After the powder is crushed, it is a multi-element microporous mineral fertilizer.
3 ) 对上述风干后的反应产物取样分析, 其有效成分含量列于表 4 ( l.OOOg矿物肥 料样品在 100ml 0.5mol/l盐酸中的溶出量, 室温, 溶解时间为 30分钟, 电磁搅拌)。 表 6实施例 7多元素微孔矿物肥料的有效成分含量 (%)
3) Sampling and analyzing the reaction products after air drying, the active ingredient content is listed in Table 4 (1.OOOg mineral fertilizer sample dissolved in 100ml 0.5mol/l hydrochloric acid, room temperature, dissolution time is 30 minutes, electromagnetic stirring) . Table 6 Example 7 Active ingredient content of multi-element microporous mineral fertilizer (%)
所用仪器: 全谱直读等离子发射光谱仪, IRIS Advantage型, 美国热电公司生产 该矿物肥料样品的烧失量为 16.20%, 块体比重为 0.755g/Cm3。 实施例 9: (40吨级工业性试验) Instrument: direct reading full spectrum of plasma emission spectrometer, IRIS Advantage type, produced by Thermo ignition loss of the mineral fertilizer sample was 16.20%, the bulk specific gravity of 0.755g / C m 3. Example 9: (40 ton industrial test)
1 ) 选取原料, 包括: 1) Select raw materials, including:
含钾硅酸盐岩石: 釆自河北省张家口市宣化, 化学组成 (%) 如下: Potassium-containing silicate rock: 宣 from Xuanhua, Zhangjiakou City, Hebei Province, chemical composition (%) is as follows:
Si02 Τί02 ΑΙΟί Fez03+Fe0 MnO CaO MgO Na20 Ρ'Λ 烧失量 合计
57. 22 0. 57 18. 34 6. 09 0. 06 0. 33 1. 12 12. 01 0. 07 0. 11 3. 60 99. 52Si0 2 Τί0 2 ΑΙΟί Fe z 0 3 +Fe0 MnO CaO MgO Na 2 0 Ρ'Λ Total loss on ignition 57. 22 0. 57 18. 34 6. 09 0. 06 0. 33 1. 12 12. 01 0. 07 0. 11 3. 60 99. 52
X射线粉晶衍射分析指出, 其矿物组成以钾长石和伊利石为主, 其它为石英等。 石灰: 含 Ca0 84%, 含 Mg0 3%, 宣化钢铁公司龙阳钙灰厂生产。 X-ray powder diffraction analysis indicates that the mineral composition is mainly potassium feldspar and illite, and the others are quartz. Lime: Contains 84% of Ca0, contains 3% of Mg0, and is produced by Xuanhua Iron and Steel Company Longyang Calcium Plant.
轻烧硼镁石: 原矿样获自辽宁天承化工厂, 将原矿粗碎样置于马弗炉内, 在 700°C 加热恒温 0.5小时, 取出, 获得物相以玻璃态为主的轻烧硼镁石矿。 Light burned boehmite: The ore sample was obtained from Liaoning Tiancheng Chemical Plant. The crude ore sample was placed in a muffle furnace, heated at 700 °C for 0.5 hour, and taken out to obtain a glass-based light burn. Boraxite ore.
2 ) 生产过程: 2) Production process:
( 1 )将含钾硅酸盐岩石、 石灰、 轻烧硼镁石分别磨细至 200目以下, 得到含钾硅 酸盐岩石粉、 石灰粉和轻烧硼镁石矿粉; 三种原料按下表比例配比: 表 7 实施例 8多元素微孔矿物肥料的原料配比
(1) grinding potassium silicate rock, lime, and light burned boehmite to below 200 mesh to obtain potassium silicate rock powder, lime powder and light burned magnesia ore powder; Proportion of the following table: Table 7 Example 8 Raw material ratio of multi-element microporous mineral fertilizer
(2 ) 首先在贮料罐中放入 1400L自来水, 然后将 10Kg轻烧硼镁石粉、 570Kg含 钾硅酸盐岩石粉、 420Kg石灰粉依次加入到水中, 并进行搅拌, 使物料混合均匀, 共 配制 40吨物料 (即配制 40罐物料)。 (2) First, put 1400L tap water in the storage tank, then add 10Kg light burned borax powder, 570Kg potassium silicate rock powder, 420Kg lime powder to the water in turn, and stir to mix the materials evenly. Formulate 40 tons of material (ie, prepare 40 cans of material).
( 3 ) 将物料转移至髙压反应釜中, 通入高压蒸气 (0.95〜1.05MPa), 在 180°C进 行水热化学反应, 反应 14小时。 (3) Transfer the material to a pressure reactor, pass high pressure steam (0.95~1.05MPa), and carry out hydrothermal chemical reaction at 180 °C for 14 hours.
(4)水热化学反应完成后降压降温冷却, 打开反应釜,取出反应产物, 自然风干, 粉碎后即得多元素微孔矿物肥料。 (4) After the completion of the hydrothermal chemical reaction, the pressure is lowered and cooled, the reaction vessel is opened, the reaction product is taken out, and it is naturally air-dried, and the elemental microporous mineral fertilizer is pulverized.
对上述风干后获得的 40吨产品用采样器从上百个点釆集肥料样品, 合并在一起, 充分混合, 用对角线四分法缩分样品至约 2kg, 并且进行系统的物质成分和显微结构 分析。 其检测结果如下: The sample of the 40 tons of product obtained after air drying is collected from hundreds of points, and combined, mixed thoroughly, and the sample is divided by a diagonal four-point method to about 2 kg, and the material composition of the system is performed. Microstructure analysis. The test results are as follows:
A. 微孔矿物肥料化学分析数据: A. Microporous mineral fertilizer chemical analysis data:
表 8 实施例 8的多元素微孔矿物肥料的主量元素含量 (wt% )
表 9 实施例 8的多元素微孔矿物肥料的微量元素含量 (mg/kg, 即 ppm)
组分 B Ba Cd Co Cr Cu Mo Ni Pb Sr V Zn 含量 559.0 262.4 3.85 10.15 58.65 5.85 10.15 53.95 10.15 216.85 141.75 81.5 所用仪器: 顺序式 X射线荧光光谱仪, XRF-1500型, 日本岛津制作所制造 Table 8 Main element content (wt%) of the multi-element microporous mineral fertilizer of Example 8. Table 9 Trace element content (mg/k g , ie ppm) of the multi-element microporous mineral fertilizer of Example 8. Component B Ba Cd Co Cr Cu Mo Ni Pb Sr V Zn Content 559.0 262.4 3.85 10.15 58.65 5.85 10.15 53.95 10.15 216.85 141.75 81.5 Apparatus used: Sequential X-ray fluorescence spectrometer, XRF-1500, manufactured by Shimadzu Corporation, Japan
B. 物相组成 B. Phase composition
经 X-射线粉晶衍射分析 (见附图 1 ), 该微孔矿物肥料由托贝莫来石 [Ca5Si6016(OH)2.4H20], 水合硅铝酸钙 [Ca3Al2(Si04)(OH)8]及碳酸钙等物相组成(所用 仪器: X-射线衍射仪, D/MAX-2400型, 日本理学电机株式会社制造)。 X-ray powder crystal diffraction analysis (see Figure 1), the microporous mineral fertilizer from tobe mullite [Ca 5 Si 6 0 16 (OH) 2 .4H 2 0], hydrated calcium aluminosilicate [Ca Phase composition of 3 Al 2 (Si0 4 )(OH) 8 ] and calcium carbonate (apparatus: X-ray diffractometer, model D/MAX-2400, manufactured by Nippon Rigaku Corporation).
C. 扫描电镜显微形态与结构的观测和分析 C. Observation and analysis of microscopic morphology and structure of scanning electron microscopy
用扫描电子显微镜(LE01450VP型, 德国里奥公司生产)对矿物肥料开展了显微 结构观察和分析,发现微孔矿物肥料的两种主要合成矿物都呈纳米 -亚微米级的微细颗 粒, 形态上一呈球状 (水合硅铝酸钙)、 另一矿物呈薄片状 (托贝莫来石), 且分布大 量微孔 (见附图 2), 因此称其为微孔矿物肥料。 Scanning electron microscopy (LE01450VP type, produced by Leo, Germany) was used to observe and analyze the microstructure of mineral fertilizers. It was found that the two main synthetic minerals of microporous mineral fertilizers are nano-submicron-sized fine particles. One is spherical (hydrated calcium aluminosilicate), the other mineral is flaky (tobe mullite), and a large number of micropores are distributed (see Figure 2), so it is called microporous mineral fertilizer.
D. 堆比重 D. Heap weight
以常规容量瓶法测定新型微孔矿物肥料的堆比重, 测定结果为 659 g/1或者 0.659 克 /立方厘米。 显然, 其比重异常的小, 这与扫描电镜显微形态观测中看到的大量微孔 分布是一致的。 The bulk specific gravity of the new microporous mineral fertilizer was determined by the conventional volumetric flask method and found to be 659 g/1 or 0.659 g/cm3. Obviously, its specific gravity is small, which is consistent with the large number of micropore distributions observed in SEM microscopic observations.
E. 0.5鹏1/1盐酸溶液中溶出组分 (亦即有效成分〉 含量的测定 E. Determination of the dissolved component (ie active ingredient) in 0.5 Peng 1/1 hydrochloric acid solution
将微孔矿物肥料研磨至 200目以下,取 1.000克试样, 置于三角瓶中, 加入 100ml Grind microporous mineral fertilizer to below 200 mesh, take 1.000 g sample, place in a triangular flask, add 100ml
0.5rnOl/l盐酸溶液, 在室温环境 (2ΓΟ下, 在电磁搅拌器上搅拌 30分钟, 过滤, 测 定滤液中溶出的成分, 结果如表 8和表 9所示: 表 10 实施例 8的多元素微孔矿物肥料的有效成分 (%)
表 11 实施例 8的多元素微孔矿物肥料的有效微量元素含量 (mg/kg, 即 ppm)
组分 B Ba Cd Co Cr Mo Ni Pb Sr V Zn Cu 含 a 458.70 78.70 0.20 2.90 23.10 2.90 30.30 2.90 211.89 94.30 18.20 0.00 所用仪器: 全谱直读等离子发射光谱仪, IRIS Advantage型, 美国热电公司生产 从上述实施例中可知, 采用本发明的水热化学反应由硅酸盐岩石制备的多元素微 孔矿物肥料含有约 4%-6%的水溶性和枸溶性 K20 (相当于一种无氯钾肥), 15%〜30% 的枸溶性硅、 30%〜40%的枸溶性钙镁、 1%〜5%的枸溶性铁以及较大比例的其它枸溶 性组分 (包括硅酸盐岩石中的各种微量元素和稀土元素)。 因此本产品是一种良好的 钾、 硅、 钙、 镁、 铁、 锰、 硼等多元素缓释长效矿物肥料。
0.5 rn O l / l hydrochloric acid solution, stirred at room temperature (2 Torr, on a magnetic stirrer for 30 minutes, filtered, and the components eluted in the filtrate were measured. The results are shown in Table 8 and Table 9: Table 10 Example 8 Active ingredient of multi-element microporous mineral fertilizer (%) Table 11 Effective trace element content (mg/kg, ie ppm) of the multi-element microporous mineral fertilizer of Example 8. Component B Ba Cd Co Cr Mo Ni Pb Sr V Zn Cu Contains a 458.70 78.70 0.20 2.90 23.10 2.90 30.30 2.90 211.89 94.30 18.20 0.00 Instrument used: Full spectrum direct reading plasma emission spectrometer, IRIS Advantage type, US Thermoelectric Company production from the above implementation As can be seen, the multi-element microporous mineral fertilizer prepared from silicate rock using the hydrothermal chemical reaction of the present invention contains about 4% to 6% of water-soluble and hydrazine-soluble K 2 0 (equivalent to a chlorine-free potassium fertilizer). , 15%~30% 枸 soluble silicon, 30%~40% 枸 soluble calcium magnesium, 1%~5% 枸 soluble iron and a large proportion of other 枸 soluble components (including each in silicate rock) Trace elements and rare earth elements). Therefore, this product is a good multi-element sustained-release long-acting mineral fertilizer such as potassium, silicon, calcium, magnesium, iron, manganese and boron.
Claims
1、一种利用水热化学反应由硅酸盐岩石制取多元素微孔矿物肥料的方法, 该方法 包括下列步骤: A method for producing a multi-element microporous mineral fertilizer from a silicate rock by hydrothermal chemical reaction, the method comprising the steps of:
( 1 ) 将硅酸盐岩石和碱土激发剂分别粉碎并磨细成粉状物料; (1) pulverizing and grinding the silicate rock and the alkaline earth activator into a powdery material;
(2) 按照 1 :0.5〜1的硅酸盐岩石: 碱土激发剂比例, 将上述粉状物料投入水中, 权 (2) According to the 1:25~1 silicate rock: alkaline earth activator ratio, the above powdery material is put into the water, right
使得水和粉状物料总重量的比例为 1〜3: 1, 并进行搅拌混合; The ratio of the total weight of the water to the powdery material is 1~3:1, and the mixture is stirred and mixed;
( 3 ) 将混合均匀的物料在封闭反应器中于 13(rC〜250°C进行水热反应, 反应时 间为 5〜24小时; (3) hydrothermally reacting the uniformly mixed material in a closed reactor at 13 °C (rC~250 ° C, the reaction time is 5 to 24 hours;
(4) 将反应产物干燥、 粉碎过筛, 即可获得多元素微孔矿物肥料, (4) The reaction product is dried, pulverized and sieved to obtain a multi-element microporous mineral fertilizer.
求 begging
其中所述的碱土激发剂包括石灰、 轻烧氧化镁和白云石灰。 The alkaline earth activators described therein include lime, light burned magnesia and dolomitic lime.
2、 根据权利要求 1所述的方法, 其中步骤 (1 ) 中的粉状物料的颗粒大小在 200 目以下。 The method according to claim 1, wherein the powdery material in the step (1) has a particle size of 200 mesh or less.
3、根据权利要求 1所述的方法,其中步骤(2〉中的水和粉状物料的重量比为 1.2〜 3. The method of claim 1 wherein the weight ratio of water to powdered material in step (2) is 1.2~
1.5: 1。 1.5: 1.
4、 根据权利要求 1所述的方法, 其中步骤 (3 ) 中的水热反应是在 170'C〜20(TC 下进行 7〜 14小时。 The method according to claim 1, wherein the hydrothermal reaction in the step (3) is carried out at 170 ° C to 20 (TC for 7 to 14 hours).
5、一种利用水热化学反应由硅酸盐岩石制取多元素微孔矿物肥料的方法, 该方法 包括下列步骤: 5. A method for producing a multi-element microporous mineral fertilizer from a silicate rock using a hydrothermal chemical reaction, the method comprising the steps of:
( 1 ) 将硅酸盐岩石、 碱土激发剂和活化剂分别粉碎并磨细成粉状物料; (1) pulverizing and grinding the silicate rock, the alkaline earth activator and the activator into a powdery material;
(2) 按照硅酸盐岩石: 碱土激发剂: 活化剂之间 1 :0.5〜1:0.01〜0.25的比例, 将 上述粉状物料投入水中, 使得水和粉状物料总重量的比例为 1 ~3: 1, 并进行搅拌混 合. (2) According to the ratio of silicate rock: alkaline earth activator: activator 1:0.5~1:0.01~0.25, put the above powdery material into water, so that the ratio of total weight of water and powdery material is 1 ~ 3: 1, and mix and mix.
(3 ) 将混合均匀的物料在封闭反应器中于 130°C〜25(TC进行水热反应, 反应时 间为 5〜24小时; (3) mixing the homogeneous material in a closed reactor at 130 ° C ~ 25 (TC hydrothermal reaction, reaction time is 5 ~ 24 hours;
(4) 将反应产物干燥、 粉碎过筛, 即可获得多元素微孔矿物肥料, (4) The reaction product is dried, pulverized and sieved to obtain a multi-element microporous mineral fertilizer.
其中所述的碱土激发剂包括石灰、 轻烧氧化镁和白云石灰, 并且所述的活化剂包- 括石膏和硼酸镁。 The alkaline earth activator described therein includes lime, light burned magnesia and dolomitic lime, and the activator comprises gypsum and magnesium borate.
6、根据权利要求 5所述的方法,其中所述的硼酸镁包括硼镁石原矿和轻烧硼镁石。
6. The method of claim 5 wherein said magnesium borate comprises boehmite ore and light burnt boehmite.
7、 根据权利要求 5所述的方法, 其中步骤 (1 ) 中的粉状物料的颗粒大小在 200 目以下。 '7. The method according to claim 5, wherein the powdery material in the step (1) has a particle size of 200 mesh or less. '
8、根据权利要求 5所述的方法,其中步骤(2)中的水和粉状物料的重量比为 1.2〜 1.5: 1。 The method according to claim 5, wherein the weight ratio of the water to the powdery material in the step (2) is from 1.2 to 1.5:1.
9、 根据权利要求 5所述的方法, 其中步骤 (3 ) 中的反应是在 170°C〜20(TC下进 行 7〜14小时。
9. The method according to claim 5, wherein the reaction in the step (3) is carried out at 170 ° C to 20 (TC for 7 to 14 hours).
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